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Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
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1

Hydrogen Production  

Fuel Cell Technologies Publication and Product Library (EERE)

This 2-page fact sheet provides a brief introduction to hydrogen production technologies. Intended for a non-technical audience, it explains how different resources and processes can be used to produ

2

FCT Hydrogen Production: Basics  

NLE Websites -- All DOE Office Websites (Extended Search)

Basics to someone by E-mail Basics to someone by E-mail Share FCT Hydrogen Production: Basics on Facebook Tweet about FCT Hydrogen Production: Basics on Twitter Bookmark FCT Hydrogen Production: Basics on Google Bookmark FCT Hydrogen Production: Basics on Delicious Rank FCT Hydrogen Production: Basics on Digg Find More places to share FCT Hydrogen Production: Basics on AddThis.com... Home Basics Central Versus Distributed Production Current Technology R&D Activities Quick Links Hydrogen Delivery Hydrogen Storage Fuel Cells Technology Validation Manufacturing Codes & Standards Education Systems Analysis Contacts Basics Photo of hydrogen production in photobioreactor Hydrogen, chemical symbol "H", is the simplest element on earth. An atom of hydrogen has only one proton and one electron. Hydrogen gas is a diatomic

3

Hydrogen Production- Current Technology  

Energy.gov (U.S. Department of Energy (DOE))

The development of clean, sustainable, and cost-competitive hydrogen production processesis key to a viable future clean energy economy. Hydrogen production technologies fall into three general...

4

FCT Hydrogen Production: Hydrogen Production R&D Activities  

NLE Websites -- All DOE Office Websites (Extended Search)

Hydrogen Production R&D Hydrogen Production R&D Activities to someone by E-mail Share FCT Hydrogen Production: Hydrogen Production R&D Activities on Facebook Tweet about FCT Hydrogen Production: Hydrogen Production R&D Activities on Twitter Bookmark FCT Hydrogen Production: Hydrogen Production R&D Activities on Google Bookmark FCT Hydrogen Production: Hydrogen Production R&D Activities on Delicious Rank FCT Hydrogen Production: Hydrogen Production R&D Activities on Digg Find More places to share FCT Hydrogen Production: Hydrogen Production R&D Activities on AddThis.com... Home Basics Current Technology R&D Activities Quick Links Hydrogen Delivery Hydrogen Storage Fuel Cells Technology Validation Manufacturing Codes & Standards Education Systems Analysis Contacts

5

Solar Hydrogen Production  

Science Journals Connector (OSTI)

The common methods of hydrogen production impose many concerns regarding the decline in...2...emission, and ecological impacts. Subsequently, all the downstream industries that consume hydrogen involve the aforem...

Ibrahim Dincer; Anand S. Joshi

2013-01-01T23:59:59.000Z

6

Hydrogen Energy System and Hydrogen Production Methods  

Science Journals Connector (OSTI)

Hydrogen is being considered as a synthetic fuel ... . This paper contains an overview of the hydrogen production methods, those being commercially available today as well...

F. Barbir; T. N. Veziro?lu

1992-01-01T23:59:59.000Z

7

Hydrogen Production from Thermocatalytic Hydrogen Sulfide Decomposition  

Science Journals Connector (OSTI)

Experimental data on hydrogen production from hydrogen sulfide decomposition over various solid catalysts at ... The possibilities given by surface modification by vacuum methods (electron beam evaporation and ma...

O. K. Alexeeva

2002-01-01T23:59:59.000Z

8

FCT Hydrogen Production: Current Technology  

NLE Websites -- All DOE Office Websites (Extended Search)

Current Technology to Current Technology to someone by E-mail Share FCT Hydrogen Production: Current Technology on Facebook Tweet about FCT Hydrogen Production: Current Technology on Twitter Bookmark FCT Hydrogen Production: Current Technology on Google Bookmark FCT Hydrogen Production: Current Technology on Delicious Rank FCT Hydrogen Production: Current Technology on Digg Find More places to share FCT Hydrogen Production: Current Technology on AddThis.com... Home Basics Current Technology Thermal Processes Electrolytic Processes Photolytic Processes R&D Activities Quick Links Hydrogen Delivery Hydrogen Storage Fuel Cells Technology Validation Manufacturing Codes & Standards Education Systems Analysis Contacts Current Technology The development of clean, sustainable, and cost-competitive hydrogen

9

Hydrogen Production Methods  

Science Journals Connector (OSTI)

As hydrogen appears to be a potential solution for a carbon-free society, its production plays a critical role in showing how well it fulfills the criteria of being environmentally benign and sustainable. Of c...

Ibrahim Dincer; Anand S. Joshi

2013-01-01T23:59:59.000Z

10

Hydrogen Production Methods  

Science Journals Connector (OSTI)

Commercially available hydrogen production methods such as steam reforming of natural gas, ... process that are based on fossil hydrocarbons and methods in the stage of development, like thermolysis ... radiolysi...

Y. Yrm

1995-01-01T23:59:59.000Z

11

Bacterial Fermentative Hydrogen Production  

Energy.gov (U.S. Department of Energy (DOE))

Presentation by Melanie Mormile, Missouri University of Science and Technology, at the Biological Hydrogen Production Workshop held September 24-25, 2013, at the National Renewable Energy Laboratory in Golden, Colorado.

12

NREL: Learning - Hydrogen Production  

NLE Websites -- All DOE Office Websites (Extended Search)

Production Production The simplest and most common element, hydrogen is all around us, but always as a compound with other elements. To make it usable in fuel cells or otherwise provide energy, we must expend energy or modify another energy source to extract it from the fossil fuel, biomass, water, or other compound in which it is found. Nearly all hydrogen production in the United States today is by steam reformation of natural gas. This, however, releases carbon dioxide in the process and trades one relatively clean fuel for another, with associated energy loss, so it does little to meet national energy needs. Hydrogen can also be produced by electrolysis-passing an electrical current through water to break it into hydrogen and oxygen-but electrolysis is inefficient and is only as clean

13

Hydrogen Production Infrastructure Options Analysis  

Energy.gov (U.S. Department of Energy (DOE))

Presentation on hydrogen production and infrastructure options presented at the DOE Transition Workshop.

14

Hydrogen Production Fact Sheet | Department of Energy  

Energy Savers (EERE)

Production Fact Sheet Hydrogen Production Fact Sheet Fact sheet produced by the Fuel Cell Technologies Office describing hydrogen production. Hydrogen Production More Documents &...

15

Resource Assessment for Hydrogen Production: Hydrogen Production...  

NLE Websites -- All DOE Office Websites (Extended Search)

Administration ERR Estimated Recoverable Reserves FCEV fuel cell electric vehicle GHG greenhouse gas GW gigawatt GWh gigawatt-hour GWdt gigawatt-days thermal H2A Hydrogen...

16

Fossil-Based Hydrogen Production  

E-Print Network (OSTI)

) Fossil-Based Hydrogen Production Praxair Praxair SNL TIAX · Integrated Ceramic Membrane System for H2

17

DOE Hydrogen Analysis Repository: Hydrogen Production by  

NLE Websites -- All DOE Office Websites (Extended Search)

Production by Photovoltaic-powered Electrolysis Production by Photovoltaic-powered Electrolysis Project Summary Full Title: Production of Hydrogen by Photovoltaic-powered Electrolysis Project ID: 91 Principal Investigator: D.L. Block Keywords: Hydrogen production; electrolysis; photovoltaic (PV) Purpose To evaluate hydrogen production from photovoltaic (PV)-powered electrolysis. Performer Principal Investigator: D.L. Block Organization: Florida Solar Energy Center Address: 1679 Clearlake Road Cocoa, FL 32922 Telephone: 321-638-1001 Email: block@fsec.ucf.edu Sponsor(s) Name: Michael Ashworth Organization: Florida Energy Office Name: Neil Rossmeissl Organization: DOE/Advanced Utilities Concepts Division Name: H.T. Everett Organization: NASA/Kennedy Space Center Project Description Type of Project: Analysis Category: Hydrogen Fuel Pathways

18

Maximizing Light Utilization Efficiency and Hydrogen Production...  

Office of Energy Efficiency and Renewable Energy (EERE) Indexed Site

in Microalgal Cultures, DOE Hydrogen Program FY 2010 Annual Progress Report Maximizing Light Utilization Efficiency and Hydrogen Production in Microalgal Cultures, DOE Hydrogen...

19

Ultraviolet stimulation of hydrogen peroxide production using...  

NLE Websites -- All DOE Office Websites (Extended Search)

Ultraviolet stimulation of hydrogen peroxide production using aminoindazole, diaminopyridine, and phenylenediamine solid polymer Ultraviolet stimulation of hydrogen peroxide...

20

Waste/By-Product Hydrogen  

NLE Websites -- All DOE Office Websites (Extended Search)

WASTE/BY-PRODUCT HYDROGEN WASTE/BY-PRODUCT HYDROGEN Ruth Cox DOE/DOD Workshop January 13, 2011 January 13, 2011 Fuel Cell and Hydrogen Energy Association The Fuel Cell and Hydrogen Energy Association FCHEA ƒ Trade Association for the industry ƒ Member driven - Market focused ƒ Developers, suppliers, customers, nonprofits, government Ad ƒ Advocacy ƒ Safety and standardization ƒ Education ƒ Strategic Alliances Fuel Cell and Hydrogen Energy Association O M b Our Members 5 W t /B d t H d Waste/By-product Hydrogen Overview Overview ƒ Growing populations, rising standards of living, and increased urbanization leads to a escalating volume of waste leads to a escalating volume of waste. ƒ Huge volumes of waste are collected in dumps, creating a major environmental issue. ƒ ƒ Wastewater treatment plants generate noxious gasses that are released in Wastewater treatment plants generate noxious gasses that are released in

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


21

Hydrogen Production & Delivery  

Energy Savers (EERE)

* Address key materials needs for P&D: Membranes, Catalysts, PEC Devices, Reactors, and Tanks Hydrogen from Coal * Complete laboratory-scale development of separation and...

22

Hydrogen Production & Delivery  

Energy.gov (U.S. Department of Energy (DOE))

"2011 DOE Hydrogen and Fuel Cells Program, and Vehicle Technologies Program Annual Merit Review and Peer Evaluation H2 and Fuel Cells Plenary "

23

NREL: Hydrogen and Fuel Cells Research - Hydrogen Production and Delivery  

NLE Websites -- All DOE Office Websites (Extended Search)

Hydrogen Production and Delivery Hydrogen Production and Delivery Most of the hydrogen in the United States is produced by steam reforming of natural gas. For the near term, this production method will continue to dominate. Researchers at NREL are developing advanced processes to produce hydrogen economically from sustainable resources. NREL's hydrogen production and delivery R&D efforts, which are led by Huyen Dinh, focus on the following topics: Biological Water Splitting Fermentation Conversion of Biomass and Wastes Photoelectrochemical Water Splitting Solar Thermal Water Splitting Renewable Electrolysis Hydrogen Dispenser Hose Reliability Hydrogen Production and Delivery Pathway Analysis. Biological Water Splitting Certain photosynthetic microbes use light energy to produce hydrogen from

24

NREL: Hydrogen and Fuel Cells Research - Hydrogen Production...  

NLE Websites -- All DOE Office Websites (Extended Search)

5 Cost adjusted to 2007 dollars, accurate to two significant figures. Printable Version Hydrogen & Fuel Cells Research Home Projects Fuel Cells Hydrogen Production & Delivery...

25

Green methods for hydrogen production  

Science Journals Connector (OSTI)

This paper discusses environmentally benign and sustainable, as green, methods for hydrogen production and categorizes them based on the driving sources and applications. Some potential sources are electrical, thermal, biochemical, photonic, electro-thermal, photo-thermal, photo-electric, photo-biochemical, and thermal-biochemical. Such forms of energy can be derived from renewable sources, nuclear energy and from energy recovery processes for hydrogen production purposes. These processes are analyzed and assessed for comparison purposes. Various case studies are presented to highlight the importance of green hydrogen production methods and systems for practical applications.

Ibrahim Dincer

2012-01-01T23:59:59.000Z

26

DOE Hydrogen and Fuel Cells Program: Hydrogen Production  

NLE Websites -- All DOE Office Websites (Extended Search)

Hydrogen Production Hydrogen Production Hydrogen Delivery Hydrogen Storage Hydrogen Manufacturing Fuel Cells Applications/Technology Validation Safety Codes and Standards Education Basic Research Systems Analysis Systems Integration U.S. Department of Energy Search help Home > Hydrogen Production Printable Version Hydrogen Production Hydrogen can be produced from diverse domestic feedstocks using a variety of process technologies. Hydrogen-containing compounds such as fossil fuels, biomass or even water can be a source of hydrogen. Thermochemical processes can be used to produce hydrogen from biomass and from fossil fuels such as coal, natural gas and petroleum. Power generated from sunlight, wind and nuclear sources can be used to produce hydrogen electrolytically. Sunlight alone can also drive photolytic production of

27

Hydrogen production costs -- A survey  

SciTech Connect

Hydrogen, produced using renewable resources, is an environmentally benign energy carrier that will play a vital role in sustainable energy systems. The US Department of Energy (DOE) supports the development of cost-effective technologies for hydrogen production, storage, and utilization to facilitate the introduction of hydrogen in the energy infrastructure. International interest in hydrogen as an energy carrier is high. Research, development, and demonstration (RD and D) of hydrogen energy systems are in progress in many countries. Annex 11 of the International Energy Agency (IEA) facilitates member countries to collaborate on hydrogen RD and D projects. The United States is a member of Annex 11, and the US representative is the Program Manager of the DOE Hydrogen R and D Program. The Executive Committee of the Hydrogen Implementing Agreement in its June 1997 meeting decided to review the production costs of hydrogen via the currently commercially available processes. This report compiles that data. The methods of production are steam reforming, partial oxidation, gasification, pyrolysis, electrolysis, photochemical, photobiological, and photoelectrochemical reactions.

Basye, L.; Swaminathan, S.

1997-12-04T23:59:59.000Z

28

Distributed Hydrogen Production from Natural Gas: Independent...  

Office of Energy Efficiency and Renewable Energy (EERE) Indexed Site

Distributed Hydrogen Production from Natural Gas: Independent Review Panel Report Distributed Hydrogen Production from Natural Gas: Independent Review Panel Report Independent...

29

Hydrogen Production - Current Technology | Department of Energy  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Current Technology Hydrogen Production - Current Technology The development of clean, sustainable, and cost-competitive hydrogen production processes is key to a viable future...

30

Sustainable Hydrogen Production  

Science Journals Connector (OSTI)

...Today, hydrogen is mainly produced from natural gas via steam methane reforming, and although this process can sustain an initial...operating, or maintenance costs are included in the calculation. HHV, higher heating value. System efficiencies of commercial electrolyzers...

John A. Turner

2004-08-13T23:59:59.000Z

31

Hydrogen Production from Solar Energy  

Science Journals Connector (OSTI)

Solar energy is potentially the most abundant renewable energy resource available to us and hydrogen production from solar energy is considered to be ... ultimate solution for sustainable energy. The various methods

Engin Ture

2007-01-01T23:59:59.000Z

32

10 - Thermochemical production of hydrogen  

Science Journals Connector (OSTI)

Abstract: The growing interest in hydrogen as a chemical reactant and energy carrier requires evaluation of all possible conversion processes for its production. This chapter analyses the different processes currently used for hydrogen production, together with the most promising approaches currently under development. Among the latter are thermochemical water-splitting cycles powered by renewable (sustainable) energy sources. A simplified description of the basic thermodynamic aspects of this process is presented, and some examples are presented.

A. Giaconia

2014-01-01T23:59:59.000Z

33

PHOTOCATALYTIC AND PHOTOELECTROCHEMICAL HYDROGEN PRODUCTION ON STRONTIUM TITANATE SINGLE CRYSTALS  

E-Print Network (OSTI)

HYDROGEN PRODUCTION ON STRONTIUM TITANATE SINGLE CRYSTALS F.HYDROGEN PRODUCTION ON STRONTIUM TITANATE SINGLE CRYSTALS

Wagner, F.T.

2012-01-01T23:59:59.000Z

34

8 - Photocatalytic production of hydrogen  

Science Journals Connector (OSTI)

Abstract: The photocatalytic production of hydrogen represents a fascinating way to convert and store solar energy as chemical energy, in the form of renewable hydrogen, the ideal fuel for the future. Hydrogen can be produced either by direct water splitting or by photo-reforming of organics in either liquid or gas phase. Both methods are reviewed in this chapter. Starting with a brief historical background, the most recent achievements in the field of photocatalytic hydrogen production are discussed, concerning both the development of innovative materials able to exploit a larger portion of the solar spectrum compared to traditional photocatalytic materials, and the different set-ups and devices which have been developed and tested.

G.L. Chiarello; E. Selli

2014-01-01T23:59:59.000Z

35

Photoelectrochemical Hydrogen Production  

SciTech Connect

The objectives of this project, covering two phases and an additional extension phase, were the development of thin film-based hybrid photovoltaic (PV)/photoelectrochemical (PEC) devices for solar-powered water splitting. The hybrid device, comprising a low-cost photoactive material integrated with amorphous silicon (a-Si:H or a-Si in short)-based solar cells as a driver, should be able to produce hydrogen with a 5% solar-to-hydrogen conversion efficiency (STH) and be durable for at least 500 hours. Three thin film material classes were studied and developed under this program: silicon-based compounds, copper chalcopyrite-based compounds, and metal oxides. With the silicon-based compounds, more specifically the amorphous silicon carbide (a-SiC), we achieved a STH efficiency of 3.7% when the photoelectrode was coupled to an a-Si tandem solar cell, and a STH efficiency of 6.1% when using a crystalline Si PV driver. The hybrid PV/a-SiC device tested under a current bias of -3~4 mA/cm{sup 2}, exhibited a durability of up to ~800 hours in 0.25 M H{sub 2}SO{sub 4} electrolyte. Other than the PV driver, the most critical element affecting the photocurrent (and hence the STH efficiency) of the hybrid PV/a-SiC device was the surface energetics at the a-SiC/electrolyte interface. Without surface modification, the photocurrent of the hybrid PEC device was ~1 mA/cm{sup 2} or lower due to a surface barrier that limits the extraction of photogenerated carriers. We conducted an extensive search for suitable surface modification techniques/materials, of which the deposition of low work function metal nanoparticles was the most successful. Metal nanoparticles of ruthenium (Ru), tungsten (W) or titanium (Ti) led to an anodic shift in the onset potential. We have also been able to develop hybrid devices of various configurations in a monolithic fashion and optimized the current matching via altering the energy bandgap and thickness of each constituent cell. As a result, the short-circuit photocurrent density of the hybrid device (measured in a 2-electrode configuration) increased significantly without assistance of any external bias, i.e. from ?1 mA/cm{sup 2} to ~5 mA/cm{sup 2}. With the copper chalcopyrite compounds, we have achieved a STH efficiency of 3.7% in a coplanar configuration with 3 a-Si solar cells and one CuGaSe{sub 2} photocathode. This material class exhibited good durability at a photocurrent density level of -4 mA/cm{sup 2} (5% STH equivalent) at a fixed potential (-0.45 VRHE). A poor band-edge alignment with the hydrogen evolution reaction (HER) potential was identified as the main limitation for high STH efficiency. Three new pathways have been identified to solve this issue. First, PV driver with bandgap lower than that of amorphous silicon were investigated. Crystalline silicon was identified as possible bottom cell. Mechanical stacks made with one Si solar cell and one CuGaSe{sub 2} photocathode were built. A 400 mV anodic shift was observed with the Si cell, leading to photocurrent density of -5 mA/cm{sup 2} at 0VRHE (compared to 0 mA/cm{sup 2} at the same potential without PV driver). We also investigated the use of p-n junctions to shift CuGaSe{sub 2} flatband potential anodically. Reactively sputtered zinc oxy-sulfide thin films was evaluated as n-type buffer and deposited on CuGaSe{sub 2}. Ruthenium nanoparticles were then added as HER catalyst. A 250 mV anodic shift was observed with the p-n junction, leading to photocurrent density at 0VRHE of -1.5 mA/cm{sup 2}. Combining this device with a Si solar cell in a mechanical stack configuration shifted the onset potential further (+400 mV anodically), leading to photocurrent density of -7 mA/cm{sup 2} at 0VRHE. Finally, we developed wide bandgap copper chalcopyrite thin film materials. We demonstrated that Se can be substituted with S using a simple annealing step. Photocurrent densities in the 5-6 mA/cm{sub 2} range were obtained with red 2.0eV CuInGaS{sub 2} photocathodes. With the metal oxide compounds, we have demonstrated that a WO{sub 3}-based hybrid p

Hu, Jian

2013-12-23T23:59:59.000Z

36

DOE Hydrogen Analysis Repository: Production of Hydrogen from Coal  

NLE Websites -- All DOE Office Websites (Extended Search)

Production of Hydrogen from Coal Production of Hydrogen from Coal Project Summary Full Title: Production of High Purity Hydrogen from Domestic Coal: Assessing the Techno-Economic Impact of Emerging Technologies Project ID: 265 Principal Investigator: Kristin Gerdes Brief Description: This report assesses the improvements in cost and performance of hydrogen production from domestic coal when employing emerging technologies funded by DOE. Keywords: Hydrogen production; Coal Purpose This analysis specifically evaluates replacing conventional acid gas removal (AGR) and hydrogen purification with warm gas cleanup (WGCU) and a high-temperature hydrogen membrane (HTHM) that meets DOE's 2010 and 2015 performance and cost research and development (R&D) targets. Performer Principal Investigator: Kristin Gerdes

37

Hydrogen Production Cost Estimate Using Biomass Gasification  

E-Print Network (OSTI)

Hydrogen Production Cost Estimate Using Biomass Gasification National Renewable Energy Laboratory% postconsumer waste #12;i Independent Review Panel Summary Report September 28, 2011 From: Independent Review Panel, Hydrogen Production Cost Estimate Using Biomass Gasification To: Mr. Mark Ruth, NREL, DOE

38

A Continuous Solar Thermochemical Hydrogen Production Plant Design  

E-Print Network (OSTI)

powered by solar thermal energy for hydrogen production. TheHydrogen Production by Concentrated Solar Energy, Energy,for hydrogen production driven by solar thermal energy is a

Luc, Wesley Wai

39

COMBINATORIAL DISCOVERY OF PHOTOCATALYSTS FOR HYDROGEN PRODUCTION  

E-Print Network (OSTI)

the development of economical and environmentally benign hydrogen production methods and reliable storage systemsCOMBINATORIAL DISCOVERY OF PHOTOCATALYSTS FOR HYDROGEN PRODUCTION Theodore Mill, Albert Hirschon materials rapidly with appropriate band- gaps and screen them for efficient hydrogen production. The goal

40

DOE Hydrogen and Fuel Cells Program Record 12024: Hydrogen Production...  

Office of Energy Efficiency and Renewable Energy (EERE) Indexed Site

12024 Date: September 19, 2012 Title: Hydrogen Production Cost Using Low-Cost Natural Gas Originator: Sara Dillich, Todd Ramsden & Marc Melaina Approved by: Sunita Satyapal Date:...

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


41

Webinar: Hydrogen Production by Polymer Electrolyte Membrane...  

Office of Energy Efficiency and Renewable Energy (EERE) Indexed Site

Production by Polymer Electrolyte Membrane (PEM) Electrolysis-Spotlight on Giner and Proton Webinar: Hydrogen Production by Polymer Electrolyte Membrane (PEM) Electrolysis-Spotligh...

42

Low Cost Hydrogen Production Platform  

SciTech Connect

A technology and design evaluation was carried out for the development of a turnkey hydrogen production system in the range of 2.4 - 12 kg/h of hydrogen. The design is based on existing SMR technology and existing chemical processes and technologies to meet the design objectives. Consequently, the system design consists of a steam methane reformer, PSA system for hydrogen purification, natural gas compression, steam generation and all components and heat exchangers required for the production of hydrogen. The focus of the program is on packaging, system integration and an overall step change in the cost of capital required for the production of hydrogen at small scale. To assist in this effort, subcontractors were brought in to evaluate the design concepts and to assist in meeting the overall goals of the program. Praxair supplied the overall system and process design and the subcontractors were used to evaluate the components and system from a manufacturing and overall design optimization viewpoint. Design for manufacturing and assembly (DFMA) techniques, computer models and laboratory/full-scale testing of components were utilized to optimize the design during all phases of the design development. Early in the program evaluation, a review of existing Praxair hydrogen facilities showed that over 50% of the installed cost of a SMR based hydrogen plant is associated with the high temperature components (reformer, shift, steam generation, and various high temperature heat exchange). The main effort of the initial phase of the program was to develop an integrated high temperature component for these related functions. Initially, six independent concepts were developed and the processes were modeled to determine overall feasibility. The six concepts were eventually narrowed down to the highest potential concept. A US patent was awarded in February 2009 for the Praxair integrated high temperature component design. A risk analysis of the high temperature component was conducted to identify any potential design deficiency related to the concept. The analysis showed that no fundamental design flaw existed with the concept, but additional simulations and prototypes would be required to verify the design prior to fabricating a production unit. These identified risks were addressed in detail during Phase II of the development program. Along with the models of the high temperature components, a detailed process and 3D design model of the remainder of system, including PSA, compression, controls, water treatment and instrumentation was developed and evaluated. Also, in Phase II of the program, laboratory/fullscale testing of the high temperature components was completed and stable operation/control of the system was verified. The overall design specifications and test results were then used to develop accurate hydrogen costs for the optimized system. Praxair continued development and testing of the system beyond the Phase II funding provided by the DOE through the end of 2008. This additional testing is not documented in this report, but did provide significant additional data for development of a prototype system as detailed in the Phase III proposal. The estimated hydrogen product costs were developed (2007 basis) for the 4.8 kg/h system at production rates of 1, 5, 10, 100 and 1,000 units built per year. With the low cost SMR approach, the product hydrogen costs for the 4.8 kg/h units at 50 units produced per year were approximately $3.02 per kg. With increasing the volume production to 1,000 units per year, the hydrogen costs are reduced by about 12% to $2.67 per kg. The cost reduction of only 12% is a result of significant design and fabrication efficiencies being realized in all levels of production runs through utilizing the DFMA principles. A simplified and easily manufactured design does not require large production volumes to show significant cost benefits. These costs represent a significant improvement and a new benchmark in the cost to produce small volume on-site hydrogen using existing process technologies. The cost mo

Timothy M. Aaron, Jerome T. Jankowiak

2009-10-16T23:59:59.000Z

43

Hydrogen Production Technical Team Roadmap  

NLE Websites -- All DOE Office Websites (Extended Search)

Production Production Technical Team Roadmap June 2013 This roadmap is a document of the U.S. DRIVE Partnership. U.S. DRIVE (Driving Research and Innovation for Vehicle efficiency and Energy sustainability) is a voluntary, non-binding, and nonlegal partnership among the U.S. Department of Energy; USCAR, representing Chrysler Group LLC, Ford Motor Company, and General Motors; Tesla Motors; five energy companies -BP America, Chevron Corporation, Phillips 66 Company, ExxonMobil Corporation, and Shell Oil Products US; two utilities - Southern California Edison and DTE Energy; and the Electric Power Research Institute (EPRI). The Hydrogen Production Technical Team is one of 12 U.S. DRIVE technical teams ("tech teams") whose mission is to accelerate the development of pre-competitive and innovative technologies to enable

44

Hydrogen and Sulfur Production from Hydrogen Sulfide Wastes  

E-Print Network (OSTI)

HYDROGEN AND SULFUR PRODUCTION FROM HYDROGEN SULFIDE WASTES? John B.L. Harkness and Richard D. Doctor, Argonne National Laboratory, Argonne. IL ABSTRACT A new hydrogen sulfide waste-treatment process that uses microwave plasma... to be economically competitive. In addition, the experiments show-that. typical refinery acid-gas streams are compatible with the plasma process and that all by-products can be treated with existing technology. BACKGROUND In 1987, Argonne staff found the first...

Harkness, J.; Doctor, R. D.

45

Air Products Hydrogen Energy Systems  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Kiczek,Edward F. [KICZEKEF@airproducts.com] Kiczek,Edward F. [KICZEKEF@airproducts.com] Sent: Monday, April 18, 2011 7:40 PM To: Gopstein, Avi (S4) Subject: Hydrogen Infrastructure Latest Advancements Attachments: Air Products Written Comments to 2011 2012 AB118 Investment Plan.pdf Follow Up Flag: Follow up Flag Status: Flagged Categories: QTR Transparency Avi, You may recall we met in DC when the McKinsey team from Germany came to discuss the EU study on hydrogen infrastructure. At that time I mention a significant advance in infrastructure that would be announced soon. Attached is our testimony to the California Energy Commission on deploying that technology. We were awarded the project to build 9 stations in southern California with the backing of

46

Hydrogen Energy Stations: Poly-Production of Electricity, Hydrogen, and Thermal Energy  

E-Print Network (OSTI)

station is one method of hydrogen production at small andstation is one method of hydrogen production at small and

Lipman, Timothy; Brooks, Cameron

2006-01-01T23:59:59.000Z

47

DOE Hydrogen Analysis Repository: Photobiological Hydrogen Production from  

NLE Websites -- All DOE Office Websites (Extended Search)

Photobiological Hydrogen Production from Green Algae Cost Analysis Photobiological Hydrogen Production from Green Algae Cost Analysis Project Summary Full Title: Updated Cost Analysis of Photobiological Hydrogen Production from Chlamydomonas reinhardtii Green Algae: Milestone Completion Report Project ID: 110 Principal Investigator: Wade Amos Purpose This report updates the 1999 economic analysis of NREL's photobiological hydrogen production from Chlamydomonas reinhardtii. The previous study had looked mainly at incident light intensities, batch cycles and light adsorption without directly attempting to model the saturation effects seen in algal cultures. This study takes a more detailed look at the effects that cell density, light adsorption and light saturation have on algal hydrogen production. Performance estimates based on actual solar data are

48

System for thermochemical hydrogen production  

DOE Patents (OSTI)

Method and apparatus are described for joule boosting a SO/sub 3/ decomposer using electrical instead of thermal energy to heat the reactants of the high temperature SO/sub 3/ decomposition step of a thermochemical hydrogen production process driven by a tandem mirror reactor. Joule boosting the decomposer to a sufficiently high temperature from a lower temperature heat source eliminates the need for expensive catalysts and reduces the temperature and consequent materials requirements for the reactor blanket. A particular decomposer design utilizes electrically heated silicon carbide rods, at a temperature of 1250/sup 0/K, to decompose a cross flow of SO/sub 3/ gas.

Werner, R.W.; Galloway, T.R.; Krikorian, O.H.

1981-05-22T23:59:59.000Z

49

IONICALLY CONDUCTING MEMBRANES FOR HYDROGEN PRODUCTION AND  

E-Print Network (OSTI)

operating experience. #12;ELTRON RESEARCH INC. Syngas Production Rate ­ 60 mL/min cm2 @ 900°C Equivalent O2IONICALLY CONDUCTING MEMBRANES FOR HYDROGEN PRODUCTION AND SEPARATION Presented by Tony Sammells for Hydrogen Production ­ Compositions ­ Feedstocks ­ Performance ­ Key Technical Hurdles · Membranes

50

Autofermentative Biological Hydrogen Production by Cyanobacteria  

Energy.gov (U.S. Department of Energy (DOE))

Presentation by Charles Dismukes, Rutgers University, at the Biological Hydrogen Production Workshop held September 24-25, 2013, at the National Renewable Energy Laboratory in Golden, Colorado.

51

Hydrogen (H2) Production by Oxygenic Phototrophs  

Energy.gov (U.S. Department of Energy (DOE))

Presentation by Eric Hegg, Michigan State University, at the Biological Hydrogen Production Workshop held September 24-25, 2013, at the National Renewable Energy Laboratory in Golden, Colorado.

52

Hydrogenases and Barriers for Biotechnological Hydrogen Production...  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Biological Hydrogen Production Workshop held September 24-25, 2013, at the National Renewable Energy Laboratory in Golden, Colorado. bioh2workshoppeters.pdf More Documents &...

53

Technoeconomic Analysis of Photoelectrochemical (PEC) Hydrogen Production  

Fuel Cell Technologies Publication and Product Library (EERE)

This report documents the engineering and cost characteristics of four PEC hydrogen production systems selected by DOE to represent canonical embodiments of future systems.

54

Electrolytic Hydrogen Production Workshop | Department of Energy  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

OnSite High Temperature Electrolysis for Efficient Hydrogen Production from Nuclear Energy, Jim O'Brien, Idaho National Laboratory Reversible Solid Oxide Electrolysis, Randy...

55

An Overview of Hydrogen Production Technologies  

SciTech Connect

Currently, hydrogen is primarily used in the chemical industry, but in the near future it will become a significant fuel. There are many processes for hydrogen production. This paper reviews reforming (steam, partial oxidation, autothermal, plasma, and aqueous phase), pyrolysis, hydrogen from biomass, electrolysis and other methods for generating hydrogen from water, and hydrogen storage. In addition, desulfurization, water-gas-shift, and hydrogen purification methods are discussed. Basics of these processes are presented with a large number of references for the interested reader to learn more.

Holladay, Jamie D.; Hu, Jianli; King, David L.; Wang, Yong

2009-01-30T23:59:59.000Z

56

Production of Hydrogen from Peanut Shells  

NLE Websites -- All DOE Office Websites (Extended Search)

Production of Hydrogen from Peanut Shells Production of Hydrogen from Peanut Shells The goal of this project is the production of renewable hydrogen from agricultural residues, in the near-term time frame (~three years) and at a comparable cost to existing methane reforming technologies. The hydrogen produced will be blended with CNG and used to power a bus in Albany, GA. Our strategy is to produce hydrogen from biomass pyrolysis oils in conjunction with high value co-products. Activated carbon can be made from agricultural residues in a two- stage process: (1) slow pyrolysis of biomass to produce charcoal, and (2) high temperature processing to form activated carbon. The vapor by-products from the first step can be steam reformed into hydrogen. NREL has developed the technology for bio-

57

Exergetic assessment of solar hydrogen production methods  

Science Journals Connector (OSTI)

Hydrogen is a sustainable fuel option and one of the potential solutions for the current energy and environmental problems. Its eco-friendly production is really crucial for better environment and sustainable development. In this paper, various types of hydrogen production methods namely solar thermal (high temperature and low temperature), photovoltaic, photoelecrtolysis, biophotolysis etc are discussed. A brief study of various hydrogen production processes have been carried out. Various solar-based hydrogen production processes are assessed and compared for their merits and demerits in terms ofexergy efficiency and sustainability factor. For a case study the exergy efficiency of hydrogen production process and the hydrogen system is discussed in terms of sustainability.

Anand S. Joshi; Ibrahim Dincer; Bale V. Reddy

2010-01-01T23:59:59.000Z

58

Hydrogen production from microbial strains  

DOE Patents (OSTI)

The present invention is directed to a method of screening microbe strains capable of generating hydrogen. This method involves inoculating one or more microbes in a sample containing cell culture medium to form an inoculated culture medium. The inoculated culture medium is then incubated under hydrogen producing conditions. Once incubating causes the inoculated culture medium to produce hydrogen, microbes in the culture medium are identified as candidate microbe strains capable of generating hydrogen. Methods of producing hydrogen using one or more of the microbial strains identified as well as the hydrogen producing strains themselves are also disclosed.

Harwood, Caroline S; Rey, Federico E

2012-09-18T23:59:59.000Z

59

Fuel Cell Technologies Office: Hydrogen Production  

NLE Websites -- All DOE Office Websites (Extended Search)

Production Production Photo of hydrogen researcher. Hydrogen can be produced using diverse, domestic resources including fossil fuels, such as natural gas and coal (with carbon sequestration); nuclear; biomass; and other renewable energy technologies, such as wind, solar, geothermal, and hydro-electric power. The overall challenge to hydrogen production is cost reduction. For cost-competitive transportation, a key driver for energy independence, hydrogen must be comparable to conventional fuels and technologies on a per-mile basis in order to succeed in the commercial marketplace. Learn more about DOE's hydrogen cost goal and the analysis used in projecting the future cost of hydrogen. The U.S. Department of Energy supports the research and development of a wide range of technologies to produce hydrogen economically and in environmentally friendly ways.

60

DOE Hydrogen Analysis Repository: Resource Analysis for Hydrogen Production  

NLE Websites -- All DOE Office Websites (Extended Search)

Resource Analysis for Hydrogen Production Resource Analysis for Hydrogen Production Project Summary Full Title: Resource Analysis for Hydrogen Production Project ID: 282 Principal Investigator: Marc Melaina Brief Description: Analysis involves estimating energy resources required to support part of the demand generated by 100 million fuel cell electric vehicles in 2040. Performer Principal Investigator: Marc Melaina Organization: National Renewable Energy Laboratory (NREL) Address: 15013 Denver West Parkway Golden, CO 80401 Telephone: 303-275-3836 Email: marc.melaina@nrel.gov Website: http://www.nrel.gov/ Sponsor(s) Name: Fred Joseck Organization: DOE/EERE/FCTO Telephone: 202-586-7932 Email: Fred.Joseck@ee.doe.gov Website: http://www.hydrogen.energy.gov/ Period of Performance Start: October 2009 Project Description

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
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61

WASTE/BY-PRODUCT HYDROGEN DOE/DOD Workshop  

E-Print Network (OSTI)

; 6 Waste/Byproduct HydrogenWaste/By product Hydrogen Waste H2 sources include: Waste biomass: biogas Waste/Byproduct Hydrogen Waste/By product Hydrogen Fuel FlexibilityFuel Flexibility Biogas: generated

62

Dynamic simulation of nuclear hydrogen production systems  

E-Print Network (OSTI)

Nuclear hydrogen production processes have been proposed as a solution to rising CO 2 emissions and low fuel yields in the production of liquid transportation fuels. In these processes, the heat of a nuclear reactor is ...

Ramrez Muoz, Patricio D. (Patricio Dario)

2011-01-01T23:59:59.000Z

63

Alternative Fuels Data Center: Hydrogen Production and Retail Requirements  

Alternative Fuels and Advanced Vehicles Data Center (EERE)

Hydrogen Production Hydrogen Production and Retail Requirements to someone by E-mail Share Alternative Fuels Data Center: Hydrogen Production and Retail Requirements on Facebook Tweet about Alternative Fuels Data Center: Hydrogen Production and Retail Requirements on Twitter Bookmark Alternative Fuels Data Center: Hydrogen Production and Retail Requirements on Google Bookmark Alternative Fuels Data Center: Hydrogen Production and Retail Requirements on Delicious Rank Alternative Fuels Data Center: Hydrogen Production and Retail Requirements on Digg Find More places to share Alternative Fuels Data Center: Hydrogen Production and Retail Requirements on AddThis.com... More in this section... Federal State Advanced Search All Laws & Incentives Sorted by Type Hydrogen Production and Retail Requirements

64

DOE Hydrogen Analysis Repository: Centralized Hydrogen Production from Wind  

NLE Websites -- All DOE Office Websites (Extended Search)

Wind Wind Project Summary Full Title: Well-to-Wheels Case Study: Centralized Hydrogen Production from Wind Project ID: 214 Principal Investigator: Fred Joseck Keywords: Wind; hydrogen production; well-to-wheels (WTW); fuel cell vehicles (FCV); electrolysis Purpose Provide well-to-wheels energy use and emissions data on a potential pathway for producing hydrogen from wind via centralized water electrolysis. This data was used in developing the U.S. Department of Energy Hydrogen Posture Plan. Performer Principal Investigator: Fred Joseck Organization: DOE/EERE/HFCIT Address: 1000 Independence Avenue, SW Washington, DC 20585 Telephone: 202-586-7932 Email: Fred.Joseck@ee.doe.gov Additional Performers: Margaret Mann, National Renewable Energy Laboratory; Michael Wang, Argonne National Laboratory

65

DOE Hydrogen Analysis Repository: Distributed Hydrogen Production from Wind  

NLE Websites -- All DOE Office Websites (Extended Search)

from Wind from Wind Project Summary Full Title: Well-to-Wheels Case Study: Distributed Hydrogen Production from Wind Project ID: 216 Principal Investigator: Fred Joseck Keywords: Wind; hydrogen production; well-to-wheels (WTW); fuel cell vehicles (FCV); electrolysis Purpose Provide well-to-wheels energy use and emissions data on a potential pathway for producing hydrogen from wind via distributed water electrolysis. This data was used in developing the U.S. Department of Energy Hydrogen Posture Plan. Performer Principal Investigator: Fred Joseck Organization: DOE/EERE/HFCIT Address: 1000 Independence Avenue, SW Washington, DC 20585 Telephone: 202-586-7932 Email: Fred.Joseck@ee.doe.gov Additional Performers: Margaret Mann, National Renewable Energy Laboratory; Michael Wang, Argonne National Laboratory

66

Waste/By-Product Hydrogen  

Energy.gov (U.S. Department of Energy (DOE))

Presentation by Ruth Cox, Fuel Cell and Hydrogen Energy Association, at the DOE-DOD Waste-to-Energy using Fuel Cells Workshop held Jan. 13, 2011

67

Enzymatic Hydrogen Production:? Conversion of Renewable Resources for Energy Production  

Science Journals Connector (OSTI)

Enzymatic Hydrogen Production:? Conversion of Renewable Resources for Energy Production ... Steam-exploded aspen wood containing 60% cellulose was a gift from Michael Himmel of the National Renewable Energy Laboratory, Golden, Colorado. ... The previous data demonstrate that the two primary components of renewable sources of energy such as biomassglucose and xyloseare capable of oxidiation by GDH, resulting in hydrogen production if hydrogenase is present. ...

Jonathan Woodward; Kimberley A. Cordray; Robert J. Edmonston; Maria Blanco-Rivera; Susan M. Mattingly; Barbara R. Evans

1999-11-20T23:59:59.000Z

68

Hydrogen Production and Delivery Research  

SciTech Connect

In response to DOE's Solicitation for Grant Applications DE-PS36-03GO93007, 'Hydrogen Production and Delivery Research', SRI International (SRI) proposed to conduct work under Technical Topic Area 5, Advanced Electrolysis Systems; Sub-Topic 5B, High-Temperature Steam Electrolysis. We proposed to develop a prototype of a modular industrial system for low-cost generation of H{sub 2} (<$2/kg) by steam electrolysis with anodic depolarization by CO. Water will be decomposed electrochemically into H{sub 2} and O{sub 2} on the cathode side of a high-temperature electrolyzer. Oxygen ions will migrate through an oxygen-ion-conductive solid oxide electrolyte. Gas mixtures on the cathode side (H{sub 2} + H{sub 2}O) and on the anode side (CO + CO{sub 2}) will be reliably separated by the solid electrolyte. Depolarization of the anodic process will decrease the electrolysis voltage, and thus the electricity required for H{sub 2} generation and the cost of produced H{sub 2}. The process is expected to be at least 10 times more energy-efficient than low-temperature electrolysis and will generate H{sub 2} at a cost of approximately $1-$1.5/kg. The operating economics of the system can be made even more attractive by deploying it at locations where waste heat is available; using waste heat would reduce the electricity required for heating the system. Two critical targets must be achieved: an H{sub 2} production cost below $2/kg, and scalable design of the pilot H{sub 2} generation system. The project deliverables would be (1) a pilot electrolysis system for H{sub 2} generation, (2) an economic analysis, (3) a market analysis, and (4) recommendations and technical documentation for field deployment. DOE was able to provide only 200K out of 1.8M (or about 10% of awarded budget), so project was stopped abruptly.

Iouri Balachov, PhD

2007-10-15T23:59:59.000Z

69

A Continuous Solar Thermochemical Hydrogen Production Plant Design  

E-Print Network (OSTI)

11]. One method for hydrogen production is a water-splittingof various methods of hydrogen production, the Department ofOne method of reducing the cost of hydrogen production is to

Luc, Wesley Wai

70

Author's personal copy Hydrogen production by Clostridium acetobutylicum ATCC  

E-Print Network (OSTI)

. However, this method (40% headspace) has been shown to result in reduced hydrogen gas productionAuthor's personal copy Hydrogen production by Clostridium acetobutylicum ATCC 824 and megaplasmid September 2009 Available online 21 October 2009 Keywords: Fermentative hydrogen production Clostridium

71

Production of Hydrogen from Underground Coal Gasification  

DOE Patents (OSTI)

A system of obtaining hydrogen from a coal seam by providing a production well that extends into the coal seam; positioning a conduit in the production well leaving an annulus between the conduit and the coal gasification production well, the conduit having a wall; closing the annulus at the lower end to seal it from the coal gasification cavity and the syngas; providing at least a portion of the wall with a bifunctional membrane that serves the dual purpose of providing a catalyzing reaction and selectively allowing hydrogen to pass through the wall and into the annulus; and producing the hydrogen through the annulus.

Upadhye, Ravindra S. (Pleasanton, CA)

2008-10-07T23:59:59.000Z

72

HYDROGEN PRODUCTION THROUGH ELECTROLYSIS Robert J. Friedland  

E-Print Network (OSTI)

HYDROGEN PRODUCTION THROUGH ELECTROLYSIS Robert J. Friedland A. John Speranza Proton Energy Systems of the Department of Energy (DOE). Proton's goal is to drive the cost of PEM electrolysis to levels of $600 per years of the cost reduction efforts for the HOGEN 40 hydrogen generator on this program are in line

73

Fluidizable Catalysts for Hydrogen Production from Biomass  

E-Print Network (OSTI)

Fluidizable Catalysts for Hydrogen Production from Biomass Pyrolysis/Steam Reforming K. Magrini/Objective Develop and demonstrate technology to produce hydrogen from biomass at $2.90/kg plant gate price based Bio-oil aqueous fraction CO H2 CO2 H2O Trap grease Waste plastics textiles Co-processing Pyrolysis

74

Mass Production Cost Estimation of Direct Hydrogen PEM Fuel Cell...  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Mass Production Cost Estimation of Direct Hydrogen PEM Fuel Cell Systems for Transportation Applications: 2012 Update Mass Production Cost Estimation of Direct Hydrogen PEM Fuel...

75

Hydrogen, Fuel Cells, and Infrastructure Technologies FY 2003 Progress Report Photoelectrochemical Hydrogen Production  

E-Print Network (OSTI)

Hydrogen, Fuel Cells, and Infrastructure Technologies FY 2003 Progress Report 1 addresses the following technical barriers from the Hydrogen Production section of the Hydrogen, Fuel Cells Photoelectrodes ." #12;Hydrogen, Fuel Cells, and Infrastructure Technologies FY 2003 Progress Report 2

76

Renewable Hydrogen Production from Biological Systems  

Energy.gov (U.S. Department of Energy (DOE))

Presentation by Matthew Posewitz, Colorado School of Mines, at the Biological Hydrogen Production Workshop held September 24-25, 2013, at the National Renewable Energy Laboratory in Golden, Colorado.

77

Hydrogen Fuel Production by Transgenic Microalgae  

Science Journals Connector (OSTI)

This chapter summarizes the state-of-art in the field of green algal H2-production and examines physiological and genetic engineering approaches by which to improve the hydrogen metabolism characteristics of thes...

Anastasios Melis; Michael Seibert

2007-01-01T23:59:59.000Z

78

Fuel Cell Technologies Office: Biological Hydrogen Production Workshop  

NLE Websites -- All DOE Office Websites (Extended Search)

Biological Hydrogen Biological Hydrogen Production Workshop to someone by E-mail Share Fuel Cell Technologies Office: Biological Hydrogen Production Workshop on Facebook Tweet about Fuel Cell Technologies Office: Biological Hydrogen Production Workshop on Twitter Bookmark Fuel Cell Technologies Office: Biological Hydrogen Production Workshop on Google Bookmark Fuel Cell Technologies Office: Biological Hydrogen Production Workshop on Delicious Rank Fuel Cell Technologies Office: Biological Hydrogen Production Workshop on Digg Find More places to share Fuel Cell Technologies Office: Biological Hydrogen Production Workshop on AddThis.com... Publications Program Publications Technical Publications Educational Publications Newsletter Program Presentations Multimedia Conferences & Meetings

79

Alternative Fuels Data Center: Hydrogen Production and Distribution  

Alternative Fuels and Advanced Vehicles Data Center (EERE)

Production Production and Distribution to someone by E-mail Share Alternative Fuels Data Center: Hydrogen Production and Distribution on Facebook Tweet about Alternative Fuels Data Center: Hydrogen Production and Distribution on Twitter Bookmark Alternative Fuels Data Center: Hydrogen Production and Distribution on Google Bookmark Alternative Fuels Data Center: Hydrogen Production and Distribution on Delicious Rank Alternative Fuels Data Center: Hydrogen Production and Distribution on Digg Find More places to share Alternative Fuels Data Center: Hydrogen Production and Distribution on AddThis.com... More in this section... Hydrogen Basics Production & Distribution Research & Development Related Links Benefits & Considerations Stations Vehicles Laws & Incentives

80

Efficient Hydrogen Production Using Enzymes of the Pentose Phosphate Pathway  

E-Print Network (OSTI)

initiated on a novel method for practical implementation of enzymes for production of hydrogen Methods of Hydrogen Production The currently used commercial methods for the production of hydrogen are inadequate for utilization of hydrogen as a fuel for transportation and electricity production. These methods

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


81

Hydrogen Production: Overview of Technology Options, January 2009  

Fuel Cell Technologies Publication and Product Library (EERE)

Overview of technology options for hydrogen production, its challenges and research needs and next steps

82

Fuel Cell Technologies Office: Biological Hydrogen Production Workshop  

NLE Websites -- All DOE Office Websites (Extended Search)

Biological Hydrogen Production Workshop Biological Hydrogen Production Workshop The U.S. Department of Energy's (DOE's) National Renewable Energy Laboratory (NREL) held a Biological Hydrogen Production Workshop on September 24-25, 2013, in Golden, Colorado. The workshop featured 29 participants representing academia, government, and national laboratories with expertise in the relevant fields. The objective of the Biological Hydrogen Production Workshop was to share information and identify issues, barriers, and research and development needs for biological hydrogen production to enable hydrogen production that meets cost goals. Proceedings 2013 Biological Hydrogen Production Workshop Final Report Presentations Introductory Session Fuel Cell Technologies Office Overview, Sara Dillich, DOE Fuel Cell Technologies Office

83

Analyzing Natural Gas Based Hydrogen Infrastructure - Optimizing Transitions from Distributed to Centralized H2 Production  

E-Print Network (OSTI)

the lowest cost hydrogen production method, supplying aroundcommon method of industrial and refinery hydrogen production

Yang, Christopher; Ogden, Joan M

2005-01-01T23:59:59.000Z

84

Four products from Escherichia coli pseudogenes increase hydrogen production q  

E-Print Network (OSTI)

Article history: Received 26 August 2013 Available online 8 September 2013 Keywords: Biohydrogen hydrogen deficiency in minimal media which suggested that the role of YlcE is associated with cell growth, and production of hydrogen as a renewable fuel is important as a means to address the problems associated

Wood, Thomas K.

85

Biological Hydrogen Production Using Synthetic Wastewater Biotin and glutamic acid are not required for biological hydrogen production.  

E-Print Network (OSTI)

Biological Hydrogen Production Using Synthetic Wastewater Conclusion ·Biotin and glutamic acid are not required for biological hydrogen production. ·MgSO4 .7H2O is a required nutrient, but hydrogen production work should focus on minimizing the lag time in biological hydrogen production, by varying nutrient

Barthelat, Francois

86

Biological Hydrogen Production Using Chloroform-treated Methanogenic Granules  

Science Journals Connector (OSTI)

In fermentative hydrogen production, the low-hydrogen-producing bacteria retention rate limits the suspended ... maintain adequate bacteria population. Traditional bacteria immobilization methods such as calcium ...

Bo Hu; Shulin Chen

2008-01-01T23:59:59.000Z

87

Biological Hydrogen Production Using Chloroform-treated Methanogenic Granules  

Science Journals Connector (OSTI)

In fermentative hydrogen production, the low-hydrogen-producing bacteria retention rate limits the suspended ... maintain adequate bacteria population. Traditional bacteria immobilization methods such as calcium ...

Bo Hu; Shulin Chen

2008-03-01T23:59:59.000Z

88

Method for the enzymatic production of hydrogen  

DOE Patents (OSTI)

The present invention is an enzymatic method for producing hydrogen comprising the steps of: (a) forming a reaction mixture within a reaction vessel comprising a substrate capable of undergoing oxidation within a catabolic reaction, such as glucose, galactose, xylose, mannose, sucrose, lactose, cellulose, xylan and starch; the reaction mixture also comprising an amount of glucose dehydrogenase in an amount sufficient to catalyze the oxidation of the substrate, an amount of hydrogenase sufficient to catalyze an electron-requiring reaction wherein a stoichiometric yield of hydrogen is produced, an amount of pH buffer in an amount sufficient to provide an environment that allows the hydrogenase and the glucose dehydrogenase to retain sufficient activity for the production of hydrogen to occur and also comprising an amount of nicotinamide adenine dinucleotide phosphate sufficient to transfer electrons from the catabolic reaction to the electron-requiring reaction; (b) heating the reaction mixture at a temperature sufficient for glucose dehydrogenase and the hydrogenase to retain sufficient activity and sufficient for the production of hydrogen to occur, and heating for a period of time that continues until the hydrogen is no longer produced by the reaction mixture, wherein the catabolic reaction and the electron-requiring reactions have rates of reaction dependent upon the temperature; and (c) detecting the hydrogen produced from the reaction mixture. 8 figs.

Woodward, J.; Mattingly, S.M.

1999-08-24T23:59:59.000Z

89

Hydrogen Production Infrastructure Options Analysis  

NLE Websites -- All DOE Office Websites (Extended Search)

Production Production Infrastructure Options Analysis January 26, 2006 Brian D. James Julie Perez Peter Schmidt (703) 243 - 3383 Brian_James@DirectedTechnologies.com Directed Technologies, Inc. Page 1 of 39 26 January 2006 2006-1-26 DOE Transition Workshop Agenda 1. Project Description and Objective 2. Team Members 3. Approach 4. Model Theory, Structure and Assumptions 5. Model Description 1. Logic 2. Features 3. Cost Components (Production, Delivery & Dispensing) 6. Los Angeles Transitional Example 7. Model Flexibility Page 2 of 39 26 January 2006 2006-1-26 DOE Transition Workshop Team Members & Interactions Start: May 2005 (effective) End: Summer 2007 * Directed Technologies, Inc.- Prime * Sentech, Inc., Research Partner * Air Products, Industrial Gas Supplier * Advisory Board * Graham Moore, Chevron Technology Ventures

90

Optical pumping production of spin polarized hydrogen  

SciTech Connect

There has been much interest recently in the production of large quantities of spin polarized hydrogen in various fields, including controlled fusion, quantum fluids, high energy, and nuclear physics. One promising method for the development of large quantities of spin polarized hydrogen is the utilization of optical pumping with a laser. Optical pumping is a process in which photon angular momentum is converted into electron and nuclear spin. The advent of tunable CW dye lasers (approx. 1 watt) allows the production of greater than 10/sup 18/ polarized atoms/sec. We have begun a program at Princeton to investigate the physics and technology of using optical pumping to produce large quantities of spin polarized hydrogen. Initial experiments have been done in small closed glass cells. Eventually, a flowing system, open target, or polarized ion source could be constructed.

Knize, R.J.; Happer, W.; Cecchi, J.L.

1984-09-01T23:59:59.000Z

91

Fuel Cell Technologies Office: Electrolysis Production of Hydrogen from  

NLE Websites -- All DOE Office Websites (Extended Search)

Electrolysis Electrolysis Production of Hydrogen from Wind and Hydropower Workshop Proceedings to someone by E-mail Share Fuel Cell Technologies Office: Electrolysis Production of Hydrogen from Wind and Hydropower Workshop Proceedings on Facebook Tweet about Fuel Cell Technologies Office: Electrolysis Production of Hydrogen from Wind and Hydropower Workshop Proceedings on Twitter Bookmark Fuel Cell Technologies Office: Electrolysis Production of Hydrogen from Wind and Hydropower Workshop Proceedings on Google Bookmark Fuel Cell Technologies Office: Electrolysis Production of Hydrogen from Wind and Hydropower Workshop Proceedings on Delicious Rank Fuel Cell Technologies Office: Electrolysis Production of Hydrogen from Wind and Hydropower Workshop Proceedings on Digg Find More places to share Fuel Cell Technologies Office:

92

Chemical Looping for Combustion and Hydrogen Production  

NLE Websites -- All DOE Office Websites (Extended Search)

ChemiCal looping for Combustion and ChemiCal looping for Combustion and hydrogen produCtion Objective The objective of this project is to determine the benefits of chemical looping technology used with coal to reduce CO 2 emissions. Background Chemical looping is a new method to convert coal or gasified coal to energy. In chemical looping, there is no direct contact between air and fuel. The chemical looping process utilizes oxygen from metal oxide oxygen carrier for fuel combustion, or for making hydrogen by "reducing" water. In combustion applications, the products of chemical looping are CO 2 and H 2 O. Thus, once the steam is condensed, a relatively pure stream of CO 2 is produced ready for sequestration. The production of a sequestration ready CO 2 stream does not require any additional separation units

93

DOE Fuel Cell Technologies Office Record 12024: Hydrogen Production...  

Office of Energy Efficiency and Renewable Energy (EERE) Indexed Site

2024: Hydrogen Production Cost Using Low-Cost Natural Gas DOE Fuel Cell Technologies Office Record 12024: Hydrogen Production Cost Using Low-Cost Natural Gas This program record...

94

Solar and Wind Technologies for Hydrogen Production Report to Congress  

Fuel Cell Technologies Publication and Product Library (EERE)

DOE's Solar and Wind Technologies for Hydrogen Production Report to Congress summarizes the technology roadmaps for solar- and wind-based hydrogen production. Published in December 2005, it fulfills t

95

An overview of hydrogen gas production from solar energy  

Science Journals Connector (OSTI)

Hydrogen production plays a very important role in the development of hydrogen economy. Hydrogen gas production through solar energy which is abundant, clean and renewable is one of the promising hydrogen production approaches. This article overviews the available technologies for hydrogen generation using solar energy as main source. Photochemical, electrochemical and thermochemical processes for producing hydrogen with solar energy are analyzed from a technological environmental and economical point of view. It is concluded that developments of improved processes for hydrogen production via solar resource are likely to continue in order to reach competitive hydrogen production costs. Hybrid thermochemical processes where hydrocarbons are exclusively used as chemical reactants for the production of syngas and the concentrated solar radiation is used as a heat source represent one of the most promising alternatives: they combine conventional and renewable energy representing a proper transition towards a solar hydrogen economy.

Simon Koumi Ngoh; Donatien Njomo

2012-01-01T23:59:59.000Z

96

Hydrogen Production from Nuclear Energy via High Temperature Electrolysis  

SciTech Connect

This paper presents the technical case for high-temperature nuclear hydrogen production. A general thermodynamic analysis of hydrogen production based on high-temperature thermal water splitting processes is presented. Specific details of hydrogen production based on high-temperature electrolysis are also provided, including results of recent experiments performed at the Idaho National Laboratory. Based on these results, high-temperature electrolysis appears to be a promising technology for efficient large-scale hydrogen production.

James E. O'Brien; Carl M. Stoots; J. Stephen Herring; Grant L. Hawkes

2006-04-01T23:59:59.000Z

97

Hydrogen Production Roadmap: Technology Pathways to the Future, January 2009  

Fuel Cell Technologies Publication and Product Library (EERE)

Roadmap to identify key challenges and priority R&D needs associated with various hydrogen fuel production technologies.

98

APPLIED GENETICS AND MOLECULAR BIOTECHNOLOGY Enhanced hydrogen production from glucose  

E-Print Network (OSTI)

(Das and Vezirolu 2001). Use of biological methods of hydrogen production should significantly reduceAPPLIED GENETICS AND MOLECULAR BIOTECHNOLOGY Enhanced hydrogen production from glucose of the metabolically engineered strains, BW25113 hyaB hybC hycA fdoG frdC ldhA aceE, increased hydrogen production 4

Wood, Thomas K.

99

Roles of cocatalysts in semiconductor-based photocatalytic hydrogen production  

Science Journals Connector (OSTI)

...cocatalyst|hydrogen production|water splitting...Photocatalytic hydrogen generation...promising way for H2 production. For water splitting...solid-state reaction method [12]. Y2O3...versus normal hydrogen electrode, negative...of CdS for H2 production could be increased...hydrothermal method through loading...

2013-01-01T23:59:59.000Z

100

Alternative Fuels Data Center: Ethanol and Hydrogen Production Facility  

Alternative Fuels and Advanced Vehicles Data Center (EERE)

Ethanol and Hydrogen Ethanol and Hydrogen Production Facility Permits to someone by E-mail Share Alternative Fuels Data Center: Ethanol and Hydrogen Production Facility Permits on Facebook Tweet about Alternative Fuels Data Center: Ethanol and Hydrogen Production Facility Permits on Twitter Bookmark Alternative Fuels Data Center: Ethanol and Hydrogen Production Facility Permits on Google Bookmark Alternative Fuels Data Center: Ethanol and Hydrogen Production Facility Permits on Delicious Rank Alternative Fuels Data Center: Ethanol and Hydrogen Production Facility Permits on Digg Find More places to share Alternative Fuels Data Center: Ethanol and Hydrogen Production Facility Permits on AddThis.com... More in this section... Federal State Advanced Search All Laws & Incentives Sorted by Type

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
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We encourage you to perform a real-time search of NLEBeta
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101

Michelangelo Network recommendations on nuclear hydrogen production  

Science Journals Connector (OSTI)

The Michelangelo Network (MICANET) was started within the 5th EURATOM Framework Programme (FP5) with the objective to elaborate a general European R&D strategy for the further development of the nuclear industry in the short, medium, and long term. To broaden the application range of nuclear power beyond dedicated electricity generation, the network proposed an orientation for future EURATOM R&D programmes including new industrial aspects of nuclear energy, such as combined heat and power and, particularly, the production of hydrogen or other fuels as a link to CO2-free energy sources. MICANET is acting as the European counterpart and partner to the Generation IV International Forum. The MICANET project ended in November 2005. Goals achieved related to nuclear hydrogen production and other non-electrical nuclear applications are outlined in this paper.

Karl Verfondern; Werner Von Lensa

2006-01-01T23:59:59.000Z

102

Startech Hydrogen Production Final Technical Report  

SciTech Connect

The assigned work scope includes the modification and utilization of the Plasma Converter System, Integration of a StarCell{trademark} Multistage Ceramic Membrane System (StarCell), and testing of the integrated systems towards DOE targets for gasification and membrane separation. Testing and evaluation was performed at the Startech Engineering and Demonstration Test Center in Bristol, CT. The Objectives of the program are as follows: (1) Characterize the performance of the integrated Plasma Converter and StarCell{trademark} Systems for hydrogen production and purification from abundant and inexpensive feedstocks; (2) Compare integrated hydrogen production performance to conventional technologies and DOE benchmarks; (3) Run pressure and temperature testing to baseline StarCell's performance; and (4) Determine the effect of process contaminants on the StarCell{trademark} system.

Startech Engineering Department

2007-11-27T23:59:59.000Z

103

NETL: News Release - DOE Advances Production of Hydrogen from Coal  

NLE Websites -- All DOE Office Websites (Extended Search)

6 , 2006 6 , 2006 DOE Advances Production of Hydrogen from Coal Projects Selected to Address Technological Challenges of Hydrogen Production in Large-Scale Facilities WASHINGTON, DC - The Department of Energy today announced the selection of six research and development projects that will promote the production of hydrogen from coal at large-scale facilities. This central approach will combat climate change by allowing for the capture - and subsequent sequestration - of carbon dioxide generated during hydrogen production. The selections support President Bush's Hydrogen Fuel Initiative, which provides funding for research and technology development to realize a future hydrogen economy that minimizes America's dependence on foreign oil and reduces greenhouse gas emissions.

104

Analysis of Hydrogen Production from Renewable Electricity Sources: Preprint  

SciTech Connect

To determine the potential for hydrogen production via renewable electricity sources, three aspects of the system are analyzed: a renewable hydrogen resource assessment, a cost analysis of hydrogen production via electrolysis, and the annual energy requirements of producing hydrogen for refueling. The results indicate that ample resources exist to produce transportation fuel from wind and solar power. However, hydrogen prices are highly dependent on electricity prices.

Levene, J. I.; Mann, M. K.; Margolis, R.; Milbrandt, A.

2005-09-01T23:59:59.000Z

105

Heat Transfer Limitations in Hydrogen Production Via Steam Reformation: The Effect of Reactor Geometry  

E-Print Network (OSTI)

Hydrogen Production and Utilization Laboratory ABSTRACT Hydrogen can be produced in a variety of methods

Vernon, David R.; Davieau, David D.; Dudgeon, Bryce A.; Erickson, Paul A.

2006-01-01T23:59:59.000Z

106

Integrated Ceramic Membrane System for Hydrogen Production  

SciTech Connect

Phase I was a technoeconomic feasibility study that defined the process scheme for the integrated ceramic membrane system for hydrogen production and determined the plan for Phase II. The hydrogen production system is comprised of an oxygen transport membrane (OTM) and a hydrogen transport membrane (HTM). Two process options were evaluated: 1) Integrated OTM-HTM reactor in this configuration, the HTM was a ceramic proton conductor operating at temperatures up to 900C, and 2) Sequential OTM and HTM reactors in this configuration, the HTM was assumed to be a Pd alloy operating at less than 600C. The analysis suggested that there are no technical issues related to either system that cannot be managed. The process with the sequential reactors was found to be more efficient, less expensive, and more likely to be commercialized in a shorter time than the single reactor. Therefore, Phase II focused on the sequential reactor system, specifically, the second stage, or the HTM portion. Work on the OTM portion was conducted in a separate program. Phase IIA began in February 2003. Candidate substrate materials and alloys were identified and porous ceramic tubes were produced and coated with Pd. Much effort was made to develop porous substrates with reasonable pore sizes suitable for Pd alloy coating. The second generation of tubes showed some improvement in pore size control, but this was not enough to get a viable membrane. Further improvements were made to the porous ceramic tube manufacturing process. When a support tube was successfully coated, the membrane was tested to determine the hydrogen flux. The results from all these tests were used to update the technoeconomic analysis from Phase I to confirm that the sequential membrane reactor system can potentially be a low-cost hydrogen supply option when using an existing membrane on a larger scale. Phase IIB began in October 2004 and focused on demonstrating an integrated HTM/water gas shift (WGS) reactor to increase CO conversion and produce more hydrogen than a standard water gas shift reactor would. Substantial improvements in substrate and membrane performance were achieved in another DOE project (DE-FC26-07NT43054). These improved membranes were used for testing in a water gas shift environment in this program. The amount of net H2 generated (defined as the difference of hydrogen produced and fed) was greater than would be produced at equilibrium using conventional water gas shift reactors up to 75 psig because of the shift in equilibrium caused by continuous hydrogen removal. However, methanation happened at higher pressures, 100 and 125 psig, and resulted in less net H2 generated than would be expected by equilibrium conversion alone. An effort to avoid methanation by testing in more oxidizing conditions (by increasing CO2/CO ratio in a feed gas) was successful and net H2 generated was higher (40-60%) than a conventional reactor at equilibrium at all pressures tested (up to 125 psig). A model was developed to predict reactor performance in both cases with and without methanation. The required membrane area depends on conditions, but the required membrane area is about 10 ft2 to produce about 2000 scfh of hydrogen. The maximum amount of hydrogen that can be produced in a membrane reactor decreased significantly due to methanation from about 2600 scfh to about 2400 scfh. Therefore, it is critical to eliminate methanation to fully benefit from the use of a membrane in the reaction. Other modeling work showed that operating a membrane reactor at higher temperature provides an opportunity to make the reactor smaller and potentially provides a significant capital cost savings compared to a shift reactor/PSA combination.

Schwartz, Joseph; Lim, Hankwon; Drnevich, Raymond

2010-08-05T23:59:59.000Z

107

Feasibility Study of Hydrogen Production at Existing Nuclear Power Plants |  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Feasibility Study of Hydrogen Production at Existing Nuclear Power Feasibility Study of Hydrogen Production at Existing Nuclear Power Plants Feasibility Study of Hydrogen Production at Existing Nuclear Power Plants A funding opportunity announcement of the cost shared feasibility studies of nuclear energy based production of hydrogen using available technology. The objective of this activity is to select and conduct project(s) that will utilize hydrogen production equipment and nuclear energy as necessary to produce data and analysis on the economics of hydrogen production with nuclear energy. Feasibility Study of Hydrogen Production at Existing Nuclear Power Plants More Documents & Publications https://e-center.doe.gov/iips/faopor.nsf/UNID/E67E46185A67EBE68 Microsoft Word - FOA cover sheet.doc Microsoft Word - hDE-FOA-0000092.rtf

108

Impact of Hydrogen Production on U.S. Energy Markets  

NLE Websites -- All DOE Office Websites (Extended Search)

Hydrogen Production on Impact of Hydrogen Production on Hydrogen Production on Impact of Hydrogen Production on U.S. Energy Markets U.S. Energy Markets Presented to: Presented to: DOE Hydrogen Transition DOE Hydrogen Transition Analysis Workshop Analysis Workshop Washington DC Washington DC January 26, 2006 January 26, 2006 Prepared by: Prepared by: E. Harry Vidas, Energy and Environmental Analysis, Inc. E. Harry Vidas, Energy and Environmental Analysis, Inc. Paul Friley, Brookhaven National Laboratory Paul Friley, Brookhaven National Laboratory AZ CA Project Scope Project Scope * Focus will be on competition between hydrogen production and distribution technologies with respect to hydrogen fuel demand, technology cost, regional mix, and impact on feedstock prices. * Evaluate impacts on U.S. energy markets including price

109

Electrochemical treatment of human waste coupled with molecular hydrogen production  

E-Print Network (OSTI)

in a hydrogen fuel cell. Herein, we report on the efficacy of a laboratory-scale wastewater electrolysis cell an electrolysis cell for on-site wastewater treatment coupled with molecular hydrogen production for useElectrochemical treatment of human waste coupled with molecular hydrogen production Kangwoo Cho

Heaton, Thomas H.

110

Production of hydrogen from oil shale  

SciTech Connect

A process for production of hydrogen from oil shale fines by direct introduction of the oil shale fines into a fluidized bed at temperatures about 1200/sup 0/ to about 2000/sup 0/ F. to obtain rapid heating of the oil shale. The bed is fluidized by upward passage of steam and oxygen, the steam introduced in the weight ratio of about 0.1 to about 10 on the basis of the organic carbon content of the oil shale and the oxygen introduced in less than the stoichiometric quantity for complete combustion of the organic carbonaceous kerogen content of the oil shale. Embodiments are disclosed for heat recovery from the spent shale and heat recovery from the spent shale and product gas wherein the complete process and heat recovery is carried out in a single reaction vessel. The process of this invention provides high conversion of organic carbon component of oil shale and high production of hydrogen from shale fines which when used in combination with a conventional oil shale hydroconversion process results in increased overall process efficiency of greater than 15 percent.

Schora, F. C.; Feldkirchner, H. L.; Janka, J. C.

1985-12-24T23:59:59.000Z

111

The economics of biological methods of hydrogen production  

E-Print Network (OSTI)

The costs to produce and utilize hydrogen are extremely high per unit of energy when compared to fossil fuel energy sources such as natural gas or gasoline. The cheapest hydrogen production approaches today are also the ...

Resnick, Richard J. (Richard Jay), 1971-

2004-01-01T23:59:59.000Z

112

Hydrogen Production R&D Activities | Department of Energy  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

R&D Activities Hydrogen Production R&D Activities An important advantage to using hydrogen as an energy carrier is that it can be produced from a variety of abundant and domestic...

113

2013 Biological Hydrogen Production Workshop Summary Report  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

is accepted as the practical maximum hydrogen yield from fermentation and actual hydrogen conversions are often even less. Other disadvantages mentioned were the impurity of the...

114

Basic Research for Hydrogen Production, Storage and Use  

NLE Websites -- All DOE Office Websites (Extended Search)

DOE Hydrogen and Fuel Cells DOE Hydrogen and Fuel Cells Coordination Meeting 6/2/2003 DOE DOE - - BES Sponsored Workshop on BES Sponsored Workshop on Basic Research for Hydrogen Basic Research for Hydrogen Production, Storage and Use Production, Storage and Use Walter J. Stevens Walter J. Stevens Director Director Chemical Sciences, Geosciences, and Biosciences Division Chemical Sciences, Geosciences, and Biosciences Division Office of Basic Energy Sciences Office of Basic Energy Sciences Workshop dates: May 13-15, 2003 A follow-on workshop to BESAC-sponsored workshop on "Basic Research Needs to Assure a Secure Energy Future" Basic Energy Sciences Basic Energy Sciences Workshop on Hydrogen Production, Storage, and Use Workshop on Hydrogen Production, Storage, and Use DOE Hydrogen and Fuel Cells

115

Hydrogen Production by the Photosynthetic Bacterium Rhodospirillum rubrum  

Science Journals Connector (OSTI)

...00/0 Hydrogen Production by the Photosynthetic...Continuous photosynthetic production ofhydrogen by Rhodospirillum...dry weight) of cells with whey as a hydrogen...processing specific organic wastes could be...in large-scale production ofhydrogen together...organisms that can use solar energy offer several...

Hans Zrrer; Reinhard Bachofen

1979-05-01T23:59:59.000Z

116

Hydrogen Gas Production from Nuclear Power Plant in Relation to Hydrogen Fuel Cell Technologies Nowadays  

Science Journals Connector (OSTI)

Recently world has been confused by issues of energy resourcing including fossil fuel use global warming and sustainable energy generation. Hydrogen may become the choice for future fuel of combustion engine. Hydrogen is an environmentally clean source of energy to end?users particularly in transportation applications because without release of pollutants at the point of end use. Hydrogen may be produced from water using the process of electrolysis. One of the GEN?IV reactors nuclear projects (HTGRs HTR VHTR) is also can produce hydrogen from the process. In the present study hydrogen gas production from nuclear power plant is reviewed in relation to commercialization of hydrogen fuel cell technologies nowadays.

2010-01-01T23:59:59.000Z

117

Hydrogen Production by Polymer Electrolyte Membrane (PEM)Electrolysis...  

Office of Energy Efficiency and Renewable Energy (EERE) Indexed Site

on Giner and Proton Presentation slides and speaker biographies from the DOE Fuel Cell Technologies Office webinar "Hydrogen Production by Polymer Electrolyte Membrane...

118

Energy Department Invests $20 Million to Advance Hydrogen Production...  

Energy Savers (EERE)

fuel cell hydrogen energy station in Fountain Valley, California. | Photo courtesy of Air Products and Chemicals. Fuel Station of the Future- Innovative Approach to Fuel Cell...

119

Technoeconomic Boundary Analysis of Biological Pathways to Hydrogen Production  

Fuel Cell Technologies Publication and Product Library (EERE)

Report documenting the biological and engineering characteristics of five algal and bacterial hydrogen production systems selected by DOE and NREL for evaluation.

120

Hydrogenases and Barriers for Biotechnological Hydrogen Production Technologies  

Energy.gov (U.S. Department of Energy (DOE))

Presentation by John Peters, Montana State University, at the Biological Hydrogen Production Workshop held September 24-25, 2013, at the National Renewable Energy Laboratory in Golden, Colorado.

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


121

Hydrogen Production and Storage for Fuel Cells: Current Status  

Energy.gov (U.S. Department of Energy (DOE))

Presented at the Clean Energy States Alliance and U.S. Department of Energy Webinar: Hydrogen Production and Storage for Fuel Cells, February 2, 2011.

122

Mesoporous electrodes for hydrogen production | Center for Bio...  

NLE Websites -- All DOE Office Websites (Extended Search)

Center News Research Highlights Center Research News Media about Center Center Video Library Bisfuel Picture Gallery Mesoporous electrodes for hydrogen production 24 Oct 2012...

123

THERMODYNAMIC EVALUATION OF PROCESSES FOR HYDROGEN PRODUCTION FROM CARBONACEOUS FUEL.  

E-Print Network (OSTI)

??This research work presents the thermodynamic analysis of hydrogen production using steam methane reforming process at different conditions. The model is developed using HSC 4.1 (more)

Kaini, Bhanu

2010-01-01T23:59:59.000Z

124

Summary of Electrolytic Hydrogen Production: Milestone Completion Report  

Energy.gov (U.S. Department of Energy (DOE))

This report provides an overview of the current state of electrolytic hydrogen production techonologies and an economic analysis of the processes and systems available as of December 2003.

125

Co-production of Hydrogen and Electricity (A Developer's Perspective)  

Energy.gov (U.S. Department of Energy (DOE))

FuelCell Energy Overview, Direct Fuel Cell (DFC) Technology Status, Hydrogen Co-production Technology, Benefits and Status, Strategic Input

126

A Continuous Solar Thermochemical Hydrogen Production Plant Design  

E-Print Network (OSTI)

Hydrogen Production Plant Heat Exchangers Turbines Electrolyzer Pumps and Compressors NaCl Storage Separators Thermochemical Reactors + Chemical Absorber Figure 6.2: Equipment Cost

Luc, Wesley Wai

127

Fermentation and Electrohydrogenic Approaches to Hydrogen Production (Presentation)  

SciTech Connect

This work describes the development of a waste biomass fermentation process using cellulose-degrading bacteria for hydrogen production. This process is then integrated with an electrohydrogenesis process via the development of a microbial electrolysis cell reactor, during which fermentation waste effluent is further converted to hydrogen to increase the total output of hydrogen from biomass.

Maness, P. C.; Thammannagowda, S.; Magnusson, L.; Logan, B.

2010-06-01T23:59:59.000Z

128

Author's personal copy Photoelectrochemical hydrogen production from water/  

E-Print Network (OSTI)

coal and gasoline [3]. Moreover, hydrogen can be used in fuel cells to generate electricity, or directly as a transportation fuel [4]. Hydrogen can be generated from hydrocarbons and water resourcesAuthor's personal copy Photoelectrochemical hydrogen production from water/ methanol decomposition

Wood, Thomas K.

129

Methane Decomposition: Production of Hydrogen and Carbon Filaments  

E-Print Network (OSTI)

for hydrogen is to power fuel cells. Major automobile manufac- turers are currently working towards developing ppm in the preferential oxidation reactor (PROX). The hydrogen can be introduced in the fuel cell only for the performance of PEM fuel cells.6 Other conventional process of hydrogen production such as partial oxidation

Goodman, Wayne

130

DOE Science Showcase - Hydrogen Production | OSTI, US Dept of Energy,  

Office of Scientific and Technical Information (OSTI)

Hydrogen Production Hydrogen Production Hydrogen Research in DOE Databases Energy Citations Database Information Bridge Science.gov WorldWideScience.org More information Making molecular hydrogen more efficiently Breaking Up (Hydrogen) No Longer As Hard To Do Hydrogen and Our Energy Future Fuel Cell Animation Hydrogen & Fuel Cells Increase your Hydrogen IQ Visit the Science Showcase homepage. OSTI Homepage Mobile Gallery Subscribe to RSS OSTI Blog Get Widgets Get Alert Services OSTI Facebook OSTI Twitter OSTI Google+ Bookmark and Share (Link will open in a new window) Go to Videos Loading... Stop news scroll Most Visited Adopt-A-Doc DOE Data Explorer DOE Green Energy DOepatents DOE R&D Accomplishments .EDUconnections Energy Science and Technology Software Center E-print Network

131

Hydrogen Production and Dispensing Facility Opens at W. Va. Airport |  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Hydrogen Production and Dispensing Facility Opens at W. Va. Airport Hydrogen Production and Dispensing Facility Opens at W. Va. Airport Hydrogen Production and Dispensing Facility Opens at W. Va. Airport August 19, 2009 - 1:00pm Addthis Major General Allen Tackett of the National Guard's 130th Airlift Wing dispenses the first fill-up of hydrogen fuel from the Yeager facility. Major General Allen Tackett of the National Guard's 130th Airlift Wing dispenses the first fill-up of hydrogen fuel from the Yeager facility. Washington, D.C. -- A hydrogen production and dispensing station constructed and operated with support from the Office of Fossil Energy's National Energy Technology Laboratory (NETL) was officially opened Monday at the Yeager Airport in Charleston, W.Va. The facility is an example of how domestically produced fuels may be used to power a variety of vehicles

132

Renewable Hydrogen Production Using Sugars and Sugar Alcohols (Presentation)  

NLE Websites -- All DOE Office Websites (Extended Search)

Working Group Meeting Working Group Meeting 11/06/2007 Renewable Hydrogen Production Using Renewable Hydrogen Production Using Sugars and Sugar Alcohols Sugars and Sugar Alcohols * * Problem: Problem: Need Need to develop renewable to develop renewable hydrogen production technologies using hydrogen production technologies using diverse diverse feedstocks feedstocks 10 15 20 CH 4 : C 6 H 14 ln(P) * * Description: Description: The BioForming The BioForming TM TM process uses process uses aqueous phase reforming to cost effectively aqueous phase reforming to cost effectively produce hydrogen from a range of feedstocks, produce hydrogen from a range of feedstocks, including glycerol and sugars. The key including glycerol and sugars. The key breakthrough is a proprietary catalyst that breakthrough is a proprietary catalyst that

133

Hydrogen Production from Hydrogen Sulfide in IGCC Power Plants  

SciTech Connect

IGCC power plants are the cleanest coal-based power generation facilities in the world. Technical improvements are needed to help make them cost competitive. Sulfur recovery is one procedure in which improvement is possible. This project has developed and demonstrated an electrochemical process that could provide such an improvement. IGCC power plants now in operation extract the sulfur from the synthesis gas as hydrogen sulfide. In this project H{sub 2}S has been electrolyzed to yield sulfur and hydrogen (instead of sulfur and water as is the present practice). The value of the byproduct hydrogen makes this process more cost effective. The electrolysis has exploited some recent developments in solid state electrolytes. The proof of principal for the project concept has been accomplished.

Elias Stefanakos; Burton Krakow; Jonathan Mbah

2007-07-31T23:59:59.000Z

134

Anti-reflective nanoporous silicon for efficient hydrogen production  

DOE Patents (OSTI)

Exemplary embodiments are disclosed of anti-reflective nanoporous silicon for efficient hydrogen production by photoelectrolysis of water. A nanoporous black Si is disclosed as an efficient photocathode for H.sub.2 production from water splitting half-reaction.

Oh, Jihun; Branz, Howard M

2014-05-20T23:59:59.000Z

135

Parametric study of solar hydrogen production from saline water electrolysis  

Science Journals Connector (OSTI)

The purpose of this work is to study the electrolysis of water for the production of hydrogen. A number of parameters, including salinity, voltage, current density and quantity of electricity, were investigated, and their effect on hydrogen production using a modified simple Hoffman electrolysis cell is reported.

S.M. El-Haggar; M. Khalil

1997-01-01T23:59:59.000Z

136

Autofermentative Biological Hydrogen Production by Cyanobacteria  

NLE Websites -- All DOE Office Websites (Extended Search)

BioSolarH BioSolarH 2  Autofermentative biological hydrogen production by cyanobacteria G.C. Dismukes Rutgers University Waksman Institute and Department of Chemistry & Chemical Biology DOE Biohydrogen Production Workshop NREL October, 2013 -BioSolarH 2  Ghirardi et al., 2007 Tamagnini et al., 2007 Soluble NiFe hydrogenase (SH) Group 5 AH in Ralstonia eutropha H16 Schäfer et al., 2013 Formate dehydrogenase Hydrogenase Bagramyan et al., 2003 Ferredoxin Km (MV) = 16.1µM Kcat (MV) = 1242 s -1 (Francis et al., 1990) K i (O 2 ) = 1% (McIntosh et al., 2011) Km (C 2 H 2 ) = 1.8*10 -3 atms (Hallenbeck et al. 1979) Km (H 2 ) =6.1µM Kcat (H 2 ) = 238 s -1 ( Schäfer et al., 2013) K i (O 2 ) = 47.5% (Lenz et al., 2010) Km (H 2 ) =3.5µM Kcat (H 2 ) = 0.5 s -1 ( Oxygen insensitive (Schäfer et al., 2013)

137

Hydrogen production from water: Recent advances in photosynthesis research  

SciTech Connect

The great potential of hydrogen production by microalgal water splitting is predicated on quantitative measurement of the algae`s hydrogen-producing capability, which is based on the following: (1) the photosynthetic unit size of hydrogen production; (2) the turnover time of photosynthetic hydrogen production; (3) thermodynamic efficiencies of conversion of light energy into the Gibbs free energy of molecular hydrogen; (4) photosynthetic hydrogen production from sea water using marine algae; (5) the potential for research advances using modern methods of molecular biology and genetic engineering to maximize hydrogen production. ORNL has shown that sustained simultaneous photoevolution of molecular hydrogen and oxygen can be performed with mutants of the green alga Chlamydomonas reinhardtii that lack a detectable level of the Photosystem I light reaction. This result is surprising in view of the standard two-light reaction model of photosynthesis and has interesting scientific and technological implications. This ORNL discovery also has potentially important implications for maximum thermodynamic conversion efficiency of light energy into chemical energy by green plant photosynthesis. Hydrogen production performed by a single light reaction, as opposed to two, implies a doubling of the theoretically maximum thermodynamic conversion efficiency from {approx}10% to {approx}20%.

Greenbaum, E.; Lee, J.W. [Oak Ridge National Lab., TN (United States). Chemical Technology Div.

1997-12-31T23:59:59.000Z

138

NETL: News Release - Hydrogen Production and Dispensing Facility Opens at  

NLE Websites -- All DOE Office Websites (Extended Search)

Hydrogen Production and Dispensing Facility Opens at West Virginia Airport Hydrogen Production and Dispensing Facility Opens at West Virginia Airport Station Provides Transportation Fuel from Domestic Resources for Hydrogen-Fueled Vehicles Washington, D.C. - A hydrogen production and dispensing station constructed and operated with support from the Office of Fossil Energy's National Energy Technology Laboratory (NETL) was officially opened Monday at the Yeager Airport in Charleston, W.Va. The facility is an example of how domestically produced fuels may be used to power a variety of vehicles and equipment, lessening U.S. dependence on foreign oil. The facility will produce, compress, store and dispense hydrogen as a fuel source for vehicles that have been converted to run on hydrogen, as well as other types of ground equipment at the airport.

139

Sandia National Laboratories: Solar Thermochemical Hydrogen Production  

NLE Websites -- All DOE Office Websites (Extended Search)

the chemical and physical transformations occurring in materials used to convert solar energy into hydrogen and develop and test novel reactor concepts at relevant scales....

140

Hydrogen production comes naturally to ocean microbe  

Science Journals Connector (OSTI)

... a multitasker it can not only photosynthesize, but can also produce large amounts of hydrogen, opening up a potential way to make the gas cheaply for fuel. The single ... to make the gas cheaply for fuel. The single-celled cyanobacterium Cyanothece 51142 can make hydrogen in air, Himadri Pakrasi of Washington University in St Louis, Missouri, and his ...

Katharine Sanderson

2010-12-14T23:59:59.000Z

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


141

Process for the production of hydrogen peroxide  

DOE Patents (OSTI)

An integrated membrane-based process method for producing hydrogen peroxide is provided comprising oxidizing hydrogenated anthraquinones with air bubbles which were created with a porous membrane, and then contacting the oxidized solution with a hydrophilic membrane to produce an organics free, H{sub 2}O{sub 2} laden permeate. 1 fig.

Datta, R.; Randhava, S.S.; Tsai, S.P.

1997-09-02T23:59:59.000Z

142

NETL: News Release - NETL Building Hydrogen Production and Dispensing  

NLE Websites -- All DOE Office Websites (Extended Search)

5, 2009 5, 2009 NETL Building Hydrogen Production and Dispensing Facility at Yeager Airport Morgantown, WV- The Department of Energy's National Energy Technology Laboratory (NETL) today announced its plans to construct and operate a hydrogen fuel production-and-dispensing facility at the Yeager Airport in Charleston, W.Va. According to U.S. Senator Robert C. Byrd, D-W.Va., "This project is a great example of the wonderful potential of coal. Coal can produce hydrogen fuel, which can greatly reduce greenhouse gases and our need to import foreign oil. Coal is abundant and remarkably versatile - particularly hydrogen produced from coal through gasification or coal-based power used to split water that provides a secure source of hydrogen fuel that will compete with imported petroleum. I am very pleased to be involved in helping this new hydrogen facility in West Virginia become a reality."

143

Ionically Conducting Membranes for Hydrogen Production and Separation  

NLE Websites -- All DOE Office Websites (Extended Search)

IONICALLY CONDUCTING MEMBRANES IONICALLY CONDUCTING MEMBRANES FOR HYDROGEN PRODUCTION AND SEPARATION Presented by Tony Sammells Eltron Research Inc. Boulder, Colorado www.eltronresearch.com Presented at DOE Hydrogen Separations Workshop Arlington, Virginia September 8, 2004 ELTRON RESEARCH INC. TO BE DISCUSSED * Membranes for Hydrogen Production - Compositions - Feedstocks - Performance - Key Technical Hurdles * Membranes for Hydrogen Separation - Compositions - Ex Situ vs. In Situ WGS - Performance - Key Technical Hurdles ELTRON RESEARCH INC. OVERALL SCHEME FOR CONVERTING FEEDSTOCK TO HYDROGEN WITH SIMULTANEOUS CARBON DIOXIDE SEQUESTRATION Oxygen Transport Membrane Hydrogen Transport Membrane Natural Gas Coal Biomass Syngas CO/H 2 WGS H 2 O CO 2 /H 2 1618afs.dsf H 2 CO 2 ELTRON RESEARCH INC. INCENTIVES FOR OXYGEN TRANSPORT MEMBRANES FOR

144

Impact of Hydrogen Production on U.S. Energy Markets | Department...  

Office of Energy Efficiency and Renewable Energy (EERE) Indexed Site

Impact of Hydrogen Production on U.S. Energy Markets Impact of Hydrogen Production on U.S. Energy Markets Presentation on the Impact of Hydrogen Production on U.S. Energy Markets...

145

Production of Large Amounts of Hydrogen Peroxide by Human Tumor Cells  

Science Journals Connector (OSTI)

...spectrophotometric method. Mouse fibroblasts...metastasis. Production of large amounts of hydrogen peroxide...sources of hydrogen peroxide production in these...MATERIALS AND METHODS Cell Lines...modified method of Ding and...width. 794 PRODUCTION OF HYDROGEN PEROXIDE...

Ted P. Szatrowski and Carl F. Nathan

1991-02-01T23:59:59.000Z

146

Hydroxyl Radical Production and Human DNA Damage Induced by Ferric Nitrilotriacetate and Hydrogen Peroxide  

Science Journals Connector (OSTI)

...to radical production by using...NTA plus hydrogen peroxide...MATERIALS AND METHODS Materials...described method (17, 18...hydroxyl radical production from hydrogen peroxide...Hydroxyl Radical Production from Hydrogen Peroxide...trapping methods were used...

Sumiko Inoue and Shosuke Kawanishi

1987-12-15T23:59:59.000Z

147

Hydrogen production with coal using a pulverization device  

DOE Patents (OSTI)

A method for producing hydrogen from coal is described wherein high temperature steam is brought into contact with coal in a pulverizer or fluid energy mill for effecting a steam-carbon reaction to provide for the generation of gaseous hydrogen. The high temperature steam is utilized to drive the coal particles into violent particle-to-particle contact for comminuting the particulates and thereby increasing the surface area of the coal particles for enhancing the productivity of the hydrogen.

Paulson, Leland E. (Morgantown, WV)

1989-01-01T23:59:59.000Z

148

Cost Analysis of a Concentrator Photovoltaic Hydrogen Production System  

SciTech Connect

The development of efficient, renewable methods of producing hydrogen are essential for the success of the hydrogen economy. Since the feedstock for electrolysis is water, there are no harmful pollutants emitted during the use of the fuel. Furthermore, it has become evident that concentrator photovoltaic (CPV) systems have a number of unique attributes that could shortcut the development process, and increase the efficiency of hydrogen production to a point where economics will then drive the commercial development to mass scale.

Thompson, J. R.; McConnell, R. D.; Mosleh, M.

2005-08-01T23:59:59.000Z

149

Process for the production of hydrogen from water  

DOE Patents (OSTI)

A method and device for the production of hydrogen from water and electricity using an active metal alloy. The active metal alloy reacts with water producing hydrogen and a metal hydroxide. The metal hydroxide is consumed, restoring the active metal alloy, by applying a voltage between the active metal alloy and the metal hydroxide. As the process is sustainable, only water and electricity is required to sustain the reaction generating hydrogen.

Miller, William E. (Naperville, IL); Maroni, Victor A. (Naperville, IL); Willit, James L. (Batavia, IL)

2010-05-25T23:59:59.000Z

150

Role prioritization of hydrogen production technologies for promoting hydrogen economy in the current state of China  

Science Journals Connector (OSTI)

Abstract Hydrogen production technologies play an important role in the hydrogen economy of China. However, the roles of different technologies played in promoting the development of hydrogen economy are different. The role prioritization of various hydrogen production technologies is of vital importance for the stakeholders/decision-makers to plan the development of hydrogen economy in China and to allocate the finite R&D budget reasonably. In this study, DPSIR framework was firstly used to identify the key factors concerning the priorities of various hydrogen production technologies; then, a fuzzy group decision-making method by incorporating fuzzy AHP and fuzzy TOPSIS was proposed to prioritize the roles of different technologies. The proposed method is capable of allowing multiple groups of stakeholders/decision-makers to participate in the decision-making and addressing problems with uncertainty and imprecise information. The prioritization results by using the proposed method demonstrated that the technologies of coal gasification with CO2 capture and storage and hydropower-based water electrolysis were regarded as the two most important hydrogen production pathways for promoting the development of hydrogen economy in China among the five assessed technologies.

Jingzheng Ren; Suzhao Gao; Shiyu Tan; Lichun Dong; Antonio Scipioni; Anna Mazzi

2015-01-01T23:59:59.000Z

151

6 - Hydrogen production by water electrolysis  

Science Journals Connector (OSTI)

Abstract: An electrolyzer combines an oxidation and a reduction reaction, driven by electricity, to produce separate streams of hydrogen gas and oxygen gas by a process called electrolysis. The hydrogen contains a portion of the electrical energy, and it can be used to generate electricity in a fuel cell by a process that is the reverse of electrolysis. If water electrolysis is driven by renewable electricity, it can be used in fuel-cell electric vehicles to displace petroleum, increase vehicle efficiency, and reduce the environmental impact of vehicles. The fundamental aspects of electrolytic hydrogen and its use as energy carrier are discussed.

N.A. Kelly

2014-01-01T23:59:59.000Z

152

On-Board Hydrogen Gas Production System For Stirling Engines  

DOE Patents (OSTI)

A hydrogen production system for use in connection with Stirling engines. The production system generates hydrogen working gas and periodically supplies it to the Stirling engine as its working fluid in instances where loss of such working fluid occurs through usage through operation of the associated Stirling engine. The hydrogen gas may be generated by various techniques including electrolysis and stored by various means including the use of a metal hydride absorbing material. By controlling the temperature of the absorbing material, the stored hydrogen gas may be provided to the Stirling engine as needed. A hydrogen production system for use in connection with Stirling engines. The production system generates hydrogen working gas and periodically supplies it to the Stirling engine as its working fluid in instances where loss of such working fluid occurs through usage through operation of the associated Stirling engine. The hydrogen gas may be generated by various techniques including electrolysis and stored by various means including the use of a metal hydride absorbing material. By controlling the temperature of the absorbing material, the stored hydrogen gas may be provided to the Stirling engine as needed.

Johansson, Lennart N. (Ann Arbor, MI)

2004-06-29T23:59:59.000Z

153

Integrating dark and light bio-hydrogen production strategies: towards the hydrogen economy  

Science Journals Connector (OSTI)

Biological methods of hydrogen production are preferable to chemical methods because of the possibility to use sunlight,...2...and organic wastes as substrates for environmentally benign conversions, under modera...

Mark D. Redwood; Marion Paterson-Beedle

2009-06-01T23:59:59.000Z

154

A Compact and Efficient Steam Methane Reformer for Hydrogen Production.  

E-Print Network (OSTI)

??A small-scale steam-methane reforming system for localized, distributed production of hydrogen offers improved performance and lower cost by integrating the following technologies developed at the (more)

Quon, Willard

2012-01-01T23:59:59.000Z

155

Hydrogen (H2) Production by Anoxygenic Purple Nonsulfur Bacteria  

Energy.gov (U.S. Department of Energy (DOE))

Presentation by Jake McKinlay, Indiana University, at the Biological Hydrogen Production Workshop held September 24-25, 2013, at the National Renewable Energy Laboratory in Golden, Colorado.

156

Hydrogen Production Cost Estimate Using Biomass Gasification: Independent Review  

Energy.gov (U.S. Department of Energy (DOE))

This independent review report assesses the 2009 state-of-the-art and 2020 projected capital cost, energy efficiency, and levelized cost for hydrogen production from biomass via gasification.

157

Photo-induced hydrogen production in a helical peptide incorporating...  

NLE Websites -- All DOE Office Websites (Extended Search)

Photo-induced hydrogen production in a helical peptide incorporating a FeFe hydrogenase active site mimic Authors: Roy, A., Madden, C., and Ghirlanda, G. Title: Photo-induced...

158

Vacancy Announcements Posted for Hydrogen Production and Delivery Program  

Energy.gov (U.S. Department of Energy (DOE))

The Fuel Cell Technologies Office has posted two vacancy announcements for a position to serve as Program Manager for the Hydrogen Production and Delivery Program in the DOE EERE Fuel Cell Technologies Office. The closing date is October 28, 2014.

159

Highly Active Steam Reforming Catalyst for Hydrogen and Syngas Production  

Science Journals Connector (OSTI)

Toyo Engineering Corporation developed a steam reforming catalyst, which is four times as active as conventional catalysts, for hydrogen and syngas production from light natural gas. The catalyst has...3 plant. B...

Toru Numaguchi

2001-11-01T23:59:59.000Z

160

DOE Hydrogen and Fuel Cells Program Record 12014: Current U.S. Hydrogen Production  

NLE Websites -- All DOE Office Websites (Extended Search)

12014 Date: June 18, 2012 12014 Date: June 18, 2012 Title: Current U.S. Hydrogen Production Originator: Fred Joseck Approved by: Sunita Satyapal Date: June 26, 2012 Item: The United States currently produces about 9 million metric tons of hydrogen per year, enough to power approximately ~36-41 million FCEVs. References/Calculations:  "...9 million metric tons of hydrogen per year" The United States produces about 9 million metric tons per year for the captive and merchant markets. U.S. Hydrogen Production By Merchant & Captive Types 2009-2016 (Thousand Metric Tons) 1 Source: MarketsandMarkets, GLOBAL HYDROGEN GENERATION MARKET BY MERCHANT & CAPTIVE TYPE, DISTRIBUTED & CENTRALIZED GENERATION, APPLICATION & TECHNOLOGY - TRENDS &

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


161

Production of Hydrogen from Peanut Shells The goal of this project is the production of renewable hydrogen from agricultural  

E-Print Network (OSTI)

developed the technology for bio- oil to hydrogen via catalytic steam reforming and shift conversion-Tech, the National Renewable Energy Laboratory has demonstrated the production of hydrogen from biomass at a flow ratio of 1.5:1 was used as a carrier gas and also as a reactant in the reformer. The test

162

NGNP Process Heat Applications: Hydrogen Production Accomplishments for FY2010  

SciTech Connect

This report summarizes FY10 accomplishments of the Next Generation Nuclear Plant (NGNP) Engineering Process Heat Applications group in support of hydrogen production technology development. This organization is responsible for systems needed to transfer high temperature heat from a high temperature gas-cooled reactor (HTGR) reactor (being developed by the INL NGNP Project) to electric power generation and to potential industrial applications including the production of hydrogen.

Charles V Park

2011-01-01T23:59:59.000Z

163

Process Intensification in Hydrogen Production from Biomass-Derived Syngas  

Science Journals Connector (OSTI)

Process Intensification in Hydrogen Production from Biomass-Derived Syngas ... A one-box process has been proposed and studied in order to economically produce pure hydrogen from biomass-derived syngas in the presence of its common impurities through the use of the water gas shift (WGS) reaction. ... (1) Hydrogen burns cleanly and produces more energy on a per mass basis than any other fuel; if widely adopted for both mobile and stationary power generation, it would reduce the emissions of pollutants typically associated with power production, and would potentially diminish the prospect of global warming. ...

Mitra Abdollahi; Jiang Yu; Hyun Tae Hwang; Paul K. T. Liu; Richard Ciora; Muhammad Sahimi; Theodore T. Tsotsis

2010-09-15T23:59:59.000Z

164

Effect of different gas releasing methods on anaerobic fermentative hydrogen production in batch cultures  

Science Journals Connector (OSTI)

Decreasing hydrogen partial pressure can not only increase the activity of the hydrogen enzyme but also decrease the products inhibition, so it is an appropriate method to enhance the fermentative hydrogen production

Sheng Chang; Jianzheng Li; Feng Liu; Ze Yu

2012-12-01T23:59:59.000Z

165

ECONOMIC FEASIBILITY ANALYSIS OF HYDROGEN PRODUCTION BY  

E-Print Network (OSTI)

. Shah and Raymond F. Drnevich Praxair, Inc. P.O. Box 44 Tonawanda, NY 14151 Abstract Praxair has on oxygen transport membrane (OTM) and hydrogen transport membrane (HTM). This system has a potential process option, both the OTM and the HTM were integrated into a single unit such that various processing

166

NREL Wind to Hydrogen Project: Renewable Hydrogen Production for Energy Storage & Transportation  

NLE Websites -- All DOE Office Websites (Extended Search)

Wind to Hydrogen Project: Wind to Hydrogen Project: Renewable Hydrogen Production for Energy Storage & Transportation NREL Hydrogen Technologies and Systems Center Todd Ramsden, Kevin Harrison, Darlene Steward November 16, 2009 NREL/PR-560-47432 NREL is a national laboratory of the U.S. Department of Energy, Office of Energy Efficiency and Renewable Energy, operated by the Alliance for Sustainable Energy, LLC. NREL Wind2H2 RD&D Project * The National Renewable Energy Laboratory in partnership with Xcel Energy and DOE has designed, operates, and continues to perform testing on the wind-to-hydrogen (Wind2H2) project at the National Wind Technology Center in Boulder * The Wind2H2 project integrates wind turbines, PV arrays and electrolyzers to produce from renewable energy

167

Hydrogen production by the decomposition of water  

DOE Patents (OSTI)

How to produce hydrogen from water was a problem addressed by this invention. The solution employs a combined electrolytical-thermochemical sulfuric acid process. Additionally, high purity sulfuric acid can be produced in the process. Water and SO.sub.2 react in electrolyzer (12) so that hydrogen is produced at the cathode and sulfuric acid is produced at the anode. Then the sulfuric acid is reacted with a particular compound M.sub.r X.sub.s so as to form at least one water insoluble sulfate and at least one water insoluble oxide of molybdenum, tungsten, or boron. Water is removed by filtration; and the sulfate is decomposed in the presence of the oxide in sulfate decomposition zone (21), thus forming SO.sub.3 and reforming M.sub.r X.sub.s. The M.sub.r X.sub.s is recycled to sulfate formation zone (16). If desired, the SO.sub.3 can be decomposed to SO.sub.2 and O.sub.2 ; and the SO.sub.2 can be recycled to electrolyzer (12) to provide a cycle for producing hydrogen.

Hollabaugh, Charles M. (Los Alamos, NM); Bowman, Melvin G. (Los Alamos, NM)

1981-01-01T23:59:59.000Z

168

Coupling a hydrogen production process to a nuclear reactor  

Science Journals Connector (OSTI)

Work is currently underway to define a pre-conceptual design of a hydrogen production plant. The reference case is a VHTR dedicated to hydrogen production using the sulphur-iodine process. The chemical part of the plant is based on a very detailed flow-sheet where all components are listed. Considering the volume and flow-rates of the circulating products, a detailed image of the chemical plant is drawn with several shops in parallel. A coupling circuit using gases was also studied with two intermediate heat exchangers at very high temperature. A specific heat transfer circuit is added inside the chemical part to distribute heat at the correct temperature. Optimisation of this circuit should lead to an increase in the overall efficiency of the process. Finally a methodology is proposed for the safety of the hydrogen production plant.

Pascal Anzieu; Patrick Aujollet; Dominique Barbier; Anne Bassi; Frederic Bertrand; Alain Le Duigou; Jean Leybros; Gilles Rodriguez

2008-01-01T23:59:59.000Z

169

Hydrogen Production from Carbohydrates: A Mini-Review  

NLE Websites -- All DOE Office Websites (Extended Search)

8 8 Hydrogen Production from Carbohydrates: A Mini-Review Y.-H. Percival Zhang *,1,2,3 1 Department of Biological Systems Engineering, Virginia Tech, 210-A Seitz Hall, Blacksburg, VA 24061, USA 2 Institute for Critical Technology and Applied Science (ICTAS), Virginia Tech, Blacksburg, VA 24061, USA 3 DOE BioEnergy Science Center (BESC), Oak Ridge, TN 37831, USA * Tel: 540-231-7414. Fax: 540-231-7414. Email: ypzhang@vt.edu. The hydrogen economy promises a clean energy future featuring higher energy utilization ef ciency and fewer pollutants compared to liquid fuel/internal combustion engines. Hydrogen production from the enriched low-cost biomass carbohydrates would achieve nearly zero carbon emissions in a whole life cycle. In this book chapter, we present latest advances of hydrogen generation from biomass carbohydrates by chemical catalysis (e.g., gasi cation,

170

Life cycle assessment of various hydrogen production methods  

Science Journals Connector (OSTI)

A comprehensive life cycle assessment (LCA) is reported for five methods of hydrogen production, namely steam reforming of natural gas, coal gasification, water electrolysis via wind and solar electrolysis, and thermochemical water splitting with a CuCl cycle. Carbon dioxide equivalent emissions and energy equivalents of each method are quantified and compared. A case study is presented for a hydrogen fueling station in Toronto, Canada, and nearby hydrogen resources close to the fueling station. In terms of carbon dioxide equivalent emissions, thermochemical water splitting with the CuCl cycle is found to be advantageous over the other methods, followed by wind and solar electrolysis. In terms of hydrogen production capacities, natural gas steam reforming, coal gasification and thermochemical water splitting with the CuCl cycle methods are found to be advantageous over the renewable energy methods.

E. Cetinkaya; I. Dincer; G.F. Naterer

2012-01-01T23:59:59.000Z

171

Discovery of Photocatalysts for Hydrogen Production  

SciTech Connect

This project for DOE was designed to address these materials-related issues through a combination of high-throughput screening of semiconductor candidates and theoretical modeling of nanostructures. High-throughput screening is an effective and economical way to examine a large number of candidates and identify those worthy of further study. Unfortunately, in the course of this project, we discovered no semiconductor candidates that can meet the DOEs stringent requirements for an economically feasible photoelectrochemical process. However, some of our results indicated that several systems may have potential if further optimized. In particular, the published theoretical modeling work indicates that core-shell nanorod structures, if properly engineered, have the potential to overcome the shortfalls of current semiconductors. Although the synthesis of the designed core-shell nanorod structures proved to be beyond the current capabilities of our laboratories, recent advances in the synthesis of core-shell nanorod structures imply that the designed structures can be synthesized. SRI is confident that once these materials are made they will validate our models and lead to economical and environmentally friendly hydrogen from sunlight and water. The high-throughput photolysis analysis module developed at SRI will also have utility in applications such as identifying catalysts for photo-assisted chemical detoxification, as well as non-photolytic applications such as hydrogen storage, which can take advantage of the ability of the analysis module to monitor pressure over time.

D. Brent MacQueen

2006-10-01T23:59:59.000Z

172

Fuel Cell Technologies Office: Electrolysis Production of Hydrogen from  

NLE Websites -- All DOE Office Websites (Extended Search)

Electrolysis Production of Hydrogen from Wind and Hydropower Workshop Proceedings Electrolysis Production of Hydrogen from Wind and Hydropower Workshop Proceedings Wind and hydropower are currently being evaluated in the U.S. and abroad as electricity sources that could enable large volume production of renewable hydrogen for use in transportation and distributed power applications. To further explore this prospect the Fuel Cell Technologies Office, and the Wind and Hydropower Technologies Program at the Department of Energy held a workshop to bring together stakeholders from wind, hydropower, and the electrolysis industries on September 9-10, 2003. The main objectives of the workshop were to: 1) discuss with stakeholders their current activities related to hydrogen, 2) explore with industry opportunities for low-cost hydrogen production through integration between wind and hydropower, water electrolysis and the electricity grid, and 3) review and provide feedback on a current Department of Energy/National Renewable Energy Laboratory analysis efforts to study opportunities for wind electrolysis and other renewable electricity sources.

173

Solar-Powered Production of Molecular Hydrogen from Water  

Science Journals Connector (OSTI)

At the present time, the majority of industrial-scale hydrogen is produced by steam?methane reformation (SMR), even though the high-temperature conversion of methane to hydrogen results in the concomitant production of carbon monoxide and carbon dioxide. ... 7-9 The PV arrays are used to convert solar light to electricity in order to power alkaline (e.g., 27% KOH at pH 14.7) electrolyzers for producing hydrogen gas. ... Narayanan et al. describe a DC-powered hybrid system that drives a methanol fuel cell in reverse,10 while Soler et al. report on a solar-powered photo-Fenton process that produces hydrogen noncatalytically under severe conditions with a limited number of organic substrates. ...

Hyunwoong Park; Chad D. Vecitis; Wonyong Choi; Oleh Weres; Michael R. Hoffmann

2008-01-04T23:59:59.000Z

174

Hydrogen Production from the Next Generation Nuclear Plant  

SciTech Connect

The Next Generation Nuclear Plant (NGNP) is a high temperature gas-cooled reactor that will be capable of producing hydrogen, electricity and/or high temperature process heat for industrial use. The project has initiated the conceptual design phase and when completed will demonstrate the viability of hydrogen generation using nuclear produced process heat. This paper explains how industry and the U.S. Government are cooperating to advance nuclear hydrogen technology. It also describes the issues being explored and the results of recent R&D including materials development and testing, thermal-fluids research, and systems analysis. The paper also describes the hydrogen production technologies being considered (including various thermochemical processes and high-temperature electrolysis).

M. Patterson; C. Park

2008-03-01T23:59:59.000Z

175

Ultrastructural Localization of Hydrogen Peroxide Production in Ligninolytic Phanerochaete chrysosporium Cells  

Science Journals Connector (OSTI)

...that H202 production activity...MATERIALS AND METHODS Organism...OF H.O. PRODUCTION IN P. CHRYSOSPORIUM...reaction, hydrogen peroxide...1972. Production of extracellular hydrogen peroxide...cytochemical methods for en...

Larry J. Forney; C. A. Reddy; H. Stuart Pankratz

1982-09-01T23:59:59.000Z

176

Hydrogen (H2) Production by Oxygenic Phototrophs  

NLE Websites -- All DOE Office Websites (Extended Search)

Production by Oxygenic Phototrophs Eric L. Hegg Michigan State University Great Lakes Bioenergy Research Center Bioresour. Technol. 2011, 102, 8589-8604 Major Challenges to H 2 Photoproduction Biological Challenges * Poor efficiency of H 2 production * Poor heterologous expression of H 2 -forming enzymes * Low quantum yields * Competition for reducing equivalents; poor electron coupling * Sensitivity of H 2 -forming enzymes to O 2 M. Ghirardi, Abstract #1751, Honolulu PRiME 2012 Technical Challenges * Mixture of H 2 and O 2 ; H 2 separation and storage * CO 2 addition and overall reactor design Overcoming Low Efficiency: Improving ET * Eliminate or down-regulate pathways competing for ele * Production of organic acids * Formation of NADPH/carbon fixation

177

Hydrogen Production Cost Estimate Using Biomass Gasification: Independent Review  

NLE Websites -- All DOE Office Websites (Extended Search)

Hydrogen Production Cost Estimate Hydrogen Production Cost Estimate Using Biomass Gasification National Renewable Energy Laboratory 1617 Cole Boulevard * Golden, Colorado 80401-3393 303-275-3000 * www.nrel.gov NREL is a national laboratory of the U.S. Department of Energy, Office of Energy Efficiency and Renewable Energy, operated by the Alliance for Sustainable Energy, LLC. Contract No. DE-AC36-08GO28308 Independent Review Published for the U.S. Department of Energy Hydrogen and Fuel Cells Program NREL/BK-6A10-51726 October 2011 NOTICE This report was prepared as an account of work sponsored by an agency of the United States government. Neither the United States government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or

178

CAPITAL AND OPERATING COST OF HYDROGEN PRODUCTION FROM COAL GASIFICATION  

NLE Websites -- All DOE Office Websites (Extended Search)

CAPITAL AND OPERATING COST OF HYDROGEN CAPITAL AND OPERATING COST OF HYDROGEN PRODUCTION FROM COAL GASIFICATION Final Report April 2003 Prepared for: The United States Department of Energy National Energy Technology Laboratory (NETL) under: Contract No. DE-AM26-99FT40465 between the NETL and Concurrent Technologies Corporation (CTC) Subcontract No. 990700362 between CTC and Parsons Infrastructure & Technology Group Inc. Task 50611 DOE Task Managers: James R. Longanbach Gary J. Stiegel Parsons Project Manager: Michael D. Rutkowski Principal Investigators: Thomas L. Buchanan Michael G. Klett Ronald L. Schoff PARSONS Capital and Operating Cost of Hydrogen Production from Coal Gasification Page i April 2003 TABLE OF CONTENTS Section Title Page List of Tables iii List of Figures iii

179

Bio-hydrogen production from renewable organic wastes  

SciTech Connect

Methane fermentation has been in practice over a century for the stabilization of high strength organic waste/wastewater. Although methanogenesis is a well established process and methane--the end-product of methanogenesis is a useful energy source; it is a low value end product with relatively less energy content (about 56 kJ energy/g CH{sub 4}). Besides, methane and its combustion by-product are powerful greenhouse gases, and responsible for global climate change. So there is a pressing need to explore alternative environmental technologies that not only stabilize the waste/wastewater but also generate benign high value end products. From this perspective, anaerobic bioconversion of organic wastes to hydrogen gas is an attractive option that achieves both goals. From energy security stand point, generation of hydrogen energy from renewable organic waste/wastewater could substitute non-renewable fossil fuels, over two-third of which is imported from politically unstable countries. Thus, biological hydrogen production from renewable organic waste through dark fermentation represents a critically important area of bioenergy production. This study evaluated both process engineering and microbial physiology of biohydrogen production.

Shihwu Sung

2004-04-30T23:59:59.000Z

180

Biological Hydrogen Production Using a Membrane Bioreactor  

E-Print Network (OSTI)

was removed, producing 2200 mg/L of cells and 500 mL/h of biogas. When operated in MBR mode, the solids. This SRT increased the overall glucose utilization (98%), the biogas production rate (640 m,800 F 600 mg/L) both increased. However, the biogas produc- tion decreased (310 F 40 m

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


181

Syngas and hydrogen production in a volumetric radiant burner  

Science Journals Connector (OSTI)

The production of syngas is the most energy demanding and metal consuming stage in the conversion of gaseous hydrocarbons (GH's) into value-added products. Its complexity restrains many practical applications of chemical processing of GH's, especially for low scale of operation. The paper describes new compact and highly productive generator of syngas and hydrogen based on the combustion of GH's in volumetric permeable matrixes with locked IR radiation that can serve as a solution of this problem. It is shown that such simple devices can provide a highly efficient methane conversion into syngas and thus facilitate the utilization of low-capacity sources of GH's for economically feasible low scale syngas and hydrogen production from various local hydrocarbon sources.

V.S. Arutyunov; V.M. Shmelev; M. Yu Sinev; O.V. Shapovalova

2011-01-01T23:59:59.000Z

182

THERMOCATALYTIC CO2-FREE PRODUCTION OF HYDROGEN FROM HYDROCARBON FUELS  

E-Print Network (OSTI)

THERMOCATALYTIC CO2- FREE PRODUCTION OF HYDROGEN FROM HYDROCARBON FUELS N. Muradov Florida Solar Energy Center 1679 Clearlake Road, Cocoa, Florida 32922 tel. 321-638-1448, fax. 321-638-1010, muradov (except for the start-up operation). This results in the following advantages: (1) no CO/CO2 byproducts

183

Hydrogen Production in a Single Chamber Microbial Electrolysis Cell  

E-Print Network (OSTI)

) at greater yields than fermentation and at greater energy efficiencies than water electrolysis. It has been to produce water. A microbial electrolysis cell (MEC) operates in a manner similar to an MFC exceptHydrogen Production in a Single Chamber Microbial Electrolysis Cell Lacking a Membrane D O U G L

184

Improving Photosynthesis for Hydrogen and Fuels Production January 24, 2011  

E-Print Network (OSTI)

Improving Photosynthesis for Hydrogen and Fuels Production January 24, 2011 Webinar Q&A Q: How do you induce hypoxic photosynthesis? I imagine you N-stress, to accumulate starch first? A to bring photosynthesis to a level lower than that of respiration. Since then, a number of labs

185

Lighting Up Enzymes for Solar Hydrogen Production (Fact Sheet)  

SciTech Connect

Scientists at the National Renewable Energy Laboratory (NREL) have combined quantum dots, which are spherical nanoparticles that possess unique size-tunable photophysical properties, with the high substrate selectivity and fast turnover of hydrogenase enzymes to achieve light-driven hydrogen (H2) production. They found that quantum dots of cadmium telluride coated in carboxylic acids easily formed highly stable complexes with the hydrogenase and that these hybrid assemblies functioned to catalyze H2 production using the energy of sunlight.

Not Available

2011-02-01T23:59:59.000Z

186

Hydrogen production using single-chamber membrane-free microbial electrolysis cells  

E-Print Network (OSTI)

efficiencies of hydrogen fuel cells in converting hydrogen to electricity. The development of advancedHydrogen production using single-chamber membrane-free microbial electrolysis cells Hongqiang Hu., Hydrogen production using single-chamber membrane-free microbial electrol- ysis cells, Water Research (2008

Tullos, Desiree

187

Co-production of Hydrogen and Electricity (A Developer's Perspective)  

NLE Websites -- All DOE Office Websites (Extended Search)

Co-production of Hydrogen and Electricity (A Developer's Perspective) Pinakin Patel FuelCell Energy, Inc. Transportation and Stationary Power Integration Workshop Fuel Cell Seminar 2008 Phoenix, AZ October 27, 2008 reliable, efficient, ultra-clean Presentation Outline * FuelCell Energy Overview * Direct Fuel Cell (DFC) Technology Status * Hydrogen Co-production Technology, Benefits and Status * Strategic Input for the DOE Workshop FCE Overview * Leading fuel cell developer for over 30 years - MCFC, SOFC, PAFC and PEM (up to 2 MW size products) - Over 230 million kWh of clean power produced world-wide (>60 installations) - Renewable fuels: over two dozen sites with ADG fuel - Ultra-clean technology: CARB-2007 certified Danbury, CT * Highly innovative approach to fuel cell development

188

Simulation Studies of Hydrogen Ion reflection from Tungsten for the Surface Production of Negative Hydrogen Ions  

SciTech Connect

The production efficiency of negative ions at tungsten surface by particle reflection has been investigated. Angular distributions and energy spectra of reflected hydrogen ions from tungsten surface are calculated with a Monte Carlo simulation code ACAT. The results obtained with ACAT have indicated that angular distributions of reflected hydrogen ions show narrow distributions for low-energy incidence such as 50 eV, and energy spectra of reflected ions show sharp peaks around 90% of incident energy. These narrow angular distributions and sharp peaks are favorable for the efficient extraction of negative ions from an ion source equipped with tungsten surface as negative ionization converter. The retained hydrogen atoms in tungsten lead to the reduction in extraction efficiency due to boarded angular distributions.

Kenmotsu, Takahiro; Wada, Motoi [Doshisha University, Kyotanabe, Kyoto 610-0394 (Japan)

2011-09-26T23:59:59.000Z

189

Hydrogen Production by the Thermophilic Alga Mastigocladus laminosus: Effects of Nitrogen, Temperature, and Inhibition of Photosynthesis  

Science Journals Connector (OSTI)

...production of hydrogen by solar radiation was also...production of hydrogen by solar radiation was also...Although there are both advantages and disadvantages to this approach...Thus, the total solar energy conversion efficiency...

Kazuhisa Miyamoto; Patrick C. Hallenbeck; John R. Benemann

1979-09-01T23:59:59.000Z

190

E-Print Network 3.0 - alternative hydrogen production Sample...  

NLE Websites -- All DOE Office Websites (Extended Search)

a number of countries have quite a substantial production of hydrogen, among these are Germany and the USA... . In the Nordic countries most of the production of hydrogen is...

191

A Conjecture on 180 Production of High Energy Hydrogen Isotopes from Nuclei  

Science Journals Connector (OSTI)

......of 1 1igh energy hydrogen isotopes in the reac...func- tion. The production cross sections of the hydrogen isotopes are well...Assuming the production cross section of...the above mentioned method, we find it tend......

Fumiyo Uchiyama

1978-03-01T23:59:59.000Z

192

Coupling of Solar Energy to Hydrogen Peroxide Production in the Cyanobacterium Anacystis nidulans  

Science Journals Connector (OSTI)

...Physiology and Biotechnology Coupling of Solar Energy to Hydrogen Peroxide Production...system for the bioconversion of solar energy. Our experimental system was based...agar and alginate. Coupling of Solar Energy to Hydrogen Peroxide Production...

Mercedes Roncel; Jos A. Navarro; Miguel A. De la Rosa

1989-02-01T23:59:59.000Z

193

Analyzing Natural Gas Based Hydrogen Infrastructure - Optimizing Transitions from Distributed to Centralized H2 Production  

E-Print Network (OSTI)

50% of daily production H 2 gas storage costs (separate fromNatural gas is currently the lowest cost hydrogen productioncosts are calculated for each station. On-site natural gas steam reformers The hydrogen production

Yang, Christopher; Ogden, Joan M

2005-01-01T23:59:59.000Z

194

Effect of gamma interferon on hydrogen peroxide production by cultured mouse peritoneal macrophages.  

Science Journals Connector (OSTI)

...increase in hydrogen peroxide production and only in...assayed by the method of Pick and...Immunol. Methods 38:161-170...superoxide and hydrogen peroxide production by macrophages...Immunol. Methods 46:211-226...

A K Sharp; D K Banerjee

1986-11-01T23:59:59.000Z

195

Photoelectrochemical Hydrogen Production Using New Combinatorial Chemistry Derived Materials  

SciTech Connect

Solar photoelectrochemical water-splitting has long been viewed as one of the holy grails of chemistry because of its potential impact as a clean, renewable method of fuel production. Several known photocatalytic semiconductors can be used; however, the fundamental mechanisms of the process remain poorly understood and no known material has the required properties for cost effective hydrogen production. In order to investigate morphological and compositional variations in metal oxides as they relate to opto-electrochemical properties, we have employed a combinatorial methodology using automated, high-throughput, electrochemical synthesis and screening together with conventional solid-state methods. This report discusses a number of novel, high-throughput instruments developed during this project for the expeditious discovery of improved materials for photoelectrochemical hydrogen production. Also described within this report are results from a variety of materials (primarily tungsten oxide, zinc oxide, molybdenum oxide, copper oxide and titanium dioxide) whose properties were modified and improved by either layering, inter-mixing, or doping with one or more transition metals. Furthermore, the morphologies of certain materials were also modified through the use of structure directing agents (SDA) during synthesis to create mesostructures (features 2-50 nm) that increased surface area and improved rates of hydrogen production.

Jaramillo, Thomas F.; Baeck, Sung-Hyeon; Kleiman-Shwarsctein, Alan; Stucky, Galen D. (PI); McFarland, Eric W. (PI)

2004-10-25T23:59:59.000Z

196

Low-Cost Hydrogen Distributed Production System Development  

SciTech Connect

H{sub 2}Gen, with the support of the Department of Energy, successfully designed, built and field-tested two steam methane reformers with 578 kg/day capacity, which has now become a standard commercial product serving customers in the specialty metals and PV manufacturing businesses. We demonstrated that this reformer/PSA system, when combined with compression, storage and dispensing (CSD) equipment could produce hydrogen that is already cost-competitive with gasoline per mile driven in a conventional (non-hybrid) vehicle. We further showed that mass producing this 578 kg/day system in quantities of just 100 units would reduce hydrogen cost per mile approximately 13% below the cost of untaxed gasoline per mile used in a hybrid electric vehicle. If mass produced in quantities of 500 units, hydrogen cost per mile in a FCEV would be 20% below the cost of untaxed gasoline in an HEV in the 2015-2020 time period using EIA fuel cost projections for natural gas and untaxed gasoline, and 45% below the cost of untaxed gasoline in a conventional car. This 20% to 45% reduction in fuel cost per mile would accrue even though hydrogen from this 578 kg/day system would cost approximately $4.14/kg, well above the DOE hydrogen cost targets of $2.50/kg by 2010 and $2.00/kg by 2015. We also estimated the cost of a larger, 1,500 kg/day SMR/PSA fueling system based on engineering cost scaling factors derived from the two H{sub 2}Gen products, a commercial 115 kg/day system and the 578 kg/day system developed under this DOE contract. This proposed system could support 200 to 250 cars per day, similar to a medium gasoline station. We estimate that the cost per mile from this larger 1,500 kg/day hydrogen fueling system would be 26% to 40% below the cost per mile of untaxed gasoline in an HEV and ICV respectively, even without any mass production cost reductions. In quantities of 500 units, we are projecting per mile cost reductions between 45% (vs. HEVs) and 62% (vs ICVs), with hydrogen costing approximately $2.87/kg, still above the DOE's 2010 $2.50/kg target. We also began laboratory testing of reforming ethanol, which we showed is currently the least expensive approach to making renewable hydrogen. Extended testing of neat ethanol in micro-reactors was successful, and we also were able to reform E-85 acquired from a local fueling station for 2,700 hours, although some modifications were required to handle the 15% gasoline present in E-85. We began initial tests of a catalyst-coated wall reformer tube that showed some promise in reducing the propensity to coke with E-85. These coated-wall tests ran for 350 hours. Additional resources would be required to commercialize an ethanol reformer operating on E-85, but there is no market for such a product at this time, so this ethanol reformer project was moth-balled pending future government or industry support. The two main objectives of this project were: (1) to design, build and test a steam methane reformer and pressure swing adsorption system that, if scaled up and mass produced, could potentially meet the DOE 2015 cost and efficiency targets for on-site distributed hydrogen generation, and (2) to demonstrate the efficacy of a low-cost renewable hydrogen generation system based on reforming ethanol to hydrogen at the fueling station.

C.E. (Sandy) Thomas, Ph.D., President; Principal Investigator, and

2011-03-10T23:59:59.000Z

197

Requirements for low cost electricity and hydrogen fuel production from multi-unit intertial fusion energy plants with a shared driver and target factory  

E-Print Network (OSTI)

achieving low CoE for hydrogen production. Although other WEfor competitive hydrogen production, such advanced targetsElectricity and Hydrogen Fuel Production from Multi-Unit

Logan, B. Grant; Moir, Ralph; Hoffman, Myron A.

1994-01-01T23:59:59.000Z

198

Overview of hydrogen production research in the Clean Energy Research Laboratory (CERL) at UOIT  

Science Journals Connector (OSTI)

Abstract This paper discusses new hydrogen production methods that have been actively investigated both theoretically and experimentally at UOIT and some recent findings through experimental measurements and analysis. A major cluster of activities at UOIT has developed novel hydrogen production systems from electrolysis to thermochemical cycles and from integrated cycles to solar-light based hydrogen production processes. The results confirm that both thermochemical cycles and photochemical processes offer promising potential for sustainable hydrogen production.

I. Dincer; G.F. Naterer

2014-01-01T23:59:59.000Z

199

Aminoguanidine inhibits aortic hydrogen peroxide production, VSMC NOX activity and hypercontractility in diabetic mice  

E-Print Network (OSTI)

hydrogen peroxide production Aortic H 2 O 2 was detected specifically using an Amplex Red Assay (details see Methods

Oak, Jeong-Ho; Youn, Ji-Youn; Cai, Hua

2009-01-01T23:59:59.000Z

200

Current (2009) State-of-the-Art Hydrogen Production Cost Estimate Using Water Electrolysis: Independent Review  

SciTech Connect

This independent review examines DOE cost targets for state-of-the art hydrogen production using water electrolysis.

Not Available

2009-09-01T23:59:59.000Z

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


201

Life Cycle Assessment of Renewable Hydrogen Production via Wind/Electrolysis: Milestone Completion Report  

Energy.gov (U.S. Department of Energy (DOE))

This report summarizes the results of a lifecycle assessment of a renewable hydrogen production process employing wind/electrolysis.

202

Updated Cost Analysis of Photobiological Hydrogen Production from Chlamydomonas reinhardtii Green Algae: Milestone Completion Report  

Energy.gov (U.S. Department of Energy (DOE))

This report updates the 1999 economic analysis of NRELs photobiological hydrogen production from Chlamydomonas reinhardtii.

203

Hydrogen Production by Noncatalytic Autothermal Reformation of Aviation Fuel Using Supercritical Water  

Science Journals Connector (OSTI)

Hydrogen Production by Noncatalytic Autothermal Reformation of Aviation Fuel Using Supercritical Water ... Energy Fuels, 2009, 23 (12), ...

Jason W. Picou; Jonathan E. Wenzel; H. Brian Lanterman; Sunggyu Lee

2009-10-07T23:59:59.000Z

204

Hydrogen Energy Stations: Poly-Production of Electricity, Hydrogen, and Thermal Energy  

E-Print Network (OSTI)

compressor Compressed hydrogen storage Figure 2: High-compressor Compressed hydrogen storage Clean Energy Group lduction, and a hydrogen compression, storage, and Energy

Lipman, Timothy; Brooks, Cameron

2006-01-01T23:59:59.000Z

205

Anthracycline Antibiotic-stimulated Superoxide, Hydrogen Peroxide, and Hydroxyl Radical Production by NADH Dehydrogenase  

Science Journals Connector (OSTI)

...ani nand hydrogen peroxide production by NADH dehydrogenase...MATERIALS AND METHODS Materials...Superoxide production by NADH dehydrogenase...with the hydrogen ion concentration...Materials and Methods." The paired...ani nand hydrogen peroxide...elicit methane production from DMSO...Materials and Methods." In these...

James H. Doroshow

1983-10-01T23:59:59.000Z

206

Short Communication High hydrogen production rate of microbial electrolysis cell (MEC) with  

E-Print Network (OSTI)

of these methods so far shown sufficient promise for economical production of hydrogen (Miyake et al., 1999; WoodShort Communication High hydrogen production rate of microbial electrolysis cell (MEC) with reduced cells (MECs) require high hydrogen production rates and a compact reactor. These goals can be achieved

207

A HYBRID ADSORBENT-MEMBRANE REACTOR (HAMR) SYSTEM FOR HYDROGEN PRODUCTION  

E-Print Network (OSTI)

hydrogen production for proton exchange membrane (PEM) fuel cells for various mobile and stationaryA HYBRID ADSORBENT-MEMBRANE REACTOR (HAMR) SYSTEM FOR HYDROGEN PRODUCTION A. Harale, H. Hwang, P recently our focus has been on new HAMR systems for hydrogen production, of potential interest to pure

Southern California, University of

208

Electron Source in Photoinduced Hydrogen Production on Pt-Supported TiO2 Particles  

Science Journals Connector (OSTI)

Electron Source in Photoinduced Hydrogen Production on Pt-Supported TiO2 Particles ... Comment on Electron Source in Photoinduced Hydrogen Production on Pt-Supported TiO2 Particles ... Comment on Electron Source in Photoinduced Hydrogen Production on Pt-Supported TiO2 Particles ...

Toshiyuki Abe; Eiji Suzuki; Kentaro Nagoshi; Kohichi Miyashita; Masao Kaneko:

2000-03-24T23:59:59.000Z

209

Technoeconomic Boundary Analysis of Biological Pathways to Hydrogen Production  

NLE Websites -- All DOE Office Websites (Extended Search)

60-46674 60-46674 September 2009 Technoeconomic Boundary Analysis of Biological Pathways to Hydrogen Production March 27, 2008 - August 31, 2009 B.D. James, G.N. Baum, J. Perez, and K.N. Baum Directed Technologies, Inc. Arlington, Virginia National Renewable Energy Laboratory 1617 Cole Boulevard, Golden, Colorado 80401-3393 303-275-3000 * www.nrel.gov NREL is a national laboratory of the U.S. Department of Energy Office of Energy Efficiency and Renewable Energy Operated by the Alliance for Sustainable Energy, LLC Contract No. DE-AC36-08-GO28308 Subcontract Report NREL/SR-560-46674 September 2009 Technoeconomic Boundary Analysis of Biological Pathways to Hydrogen Production March 27, 2008 - August 31, 2009 B.D. James, G.N. Baum, J. Perez, and K.N. Baum

210

Fuzzy Delphi method for evaluating hydrogen production technologies  

Science Journals Connector (OSTI)

The purpose of this research is to establish an evaluation model for selecting the most appropriate technology for development in Taiwan, based on 14 evaluation criteria. Due to the inherent uncertainty and imprecision associated with the mapping of decision makers perception to crisp values, linguistic variables are used to assess the weights of the criteria and the ratings of each technology with respect to each criterion. The criteria weights and technology ratings are collected through a seven-point linguistic scale using a Delphi questionnaire. The linguistic scores are then converted into fuzzy numbers, and a consensus of the decision makers opinions on weights and ratings is mathematically derived using fuzzy Delphi methodology. We have used the model to evaluate seven different hydrogen production technologies. The results indicate that hydrogen production via electrolysis by wind power and that via electrolysis by photovoltaic electricity are the two technologies that should be chosen for further development.

Pao-Long Chang; Chiung-Wen Hsu; Po-Chien Chang

2011-01-01T23:59:59.000Z

211

A NOVEL MEMBRANE REACTOR FOR DIRECT HYDROGEN PRODUCTION FROM COAL  

SciTech Connect

Gas Technology Institute is developing a novel concept of membrane reactor coupled with a gasifier for high efficiency, clean and low cost production of hydrogen from coal. The concept incorporates a hydrogen-selective membrane within a gasification reactor for direct extraction of hydrogen from coal-derived synthesis gases. The objective of this project is to determine the technical and economic feasibility of this concept by screening, testing and identifying potential candidate membranes under high temperature, high pressure, and harsh environments of the coal gasification conditions. The best performing membranes will be selected for preliminary reactor design and cost estimates. Hydrogen permeation data for several perovskite membranes BCN (BaCe{sub 0.9}Nd{sub 0.1}O{sub 3-x}), SCE (SrCe{sub 0.9}Eu{sub 0.1}O{sub 3}) and SCTm (SrCe{sub 0.95}Tm{sub 0.05}O{sub 3}) have been successfully obtained for temperatures between 800 and 950 C and pressures from 1 to 12 bar in this project. However, it is known that the cerate-based perovskite materials can react with CO{sub 2}. Therefore, the stability issue of the proton conducting perovskite materials under CO{sub 2} or H{sub 2}S environments was examined. Tests were conducted in the Thermo Gravimetric Analyzer (TGA) unit for powder and disk forms of BCN and SCE. Perovskite materials doped with zirconium (Zr) are known to be resistant to CO{sub 2}. The results from the evaluation of the chemical stability for the Zr doped perovskite membranes are presented. During this reporting period, flowsheet simulation was also performed to calculate material and energy balance based on several hydrogen production processes from coal using high temperature membrane reactor (1000 C), low temperature membrane reactor (250 C), or conventional technologies. The results show that the coal to hydrogen process employing both the high temperature and the low temperature membrane reactors can increase the hydrogen production efficiency (cold gas efficiency) by more than 50% compared to the conventional process. Using either high temperature or low temperature membrane reactor process also results in an increase of the cold gas efficiencies as well as the thermal efficiencies of the overall process.

Shain Doong; Estela Ong; Mike Atroshenko; Francis Lau; Mike Roberts

2005-07-29T23:59:59.000Z

212

Comparative Environmental Impact Evaluation of Hydrogen Production Methods from Renewable and Nonrenewable Sources  

Science Journals Connector (OSTI)

In this chapter, a comparative environmental impact study of possible hydrogen production methods from renewable and nonrenewable sources is undertaken ... potential, GWP and acidification potential, AP), production

Canan Acar; Ibrahim Dincer

2013-01-01T23:59:59.000Z

213

The development of autocatalytic structural materials for use in the sulfur-iodine process for the production of hydrogen .  

E-Print Network (OSTI)

??The Sulfur-Iodine Cycle for the thermochemical production of hydrogen offers many benefits to traditional methods of hydrogen production. As opposed to steam methane reforming - (more)

Miu, Kevin (Kevin K.)

2006-01-01T23:59:59.000Z

214

Chemical Hydride Slurry for Hydrogen Production and Storage  

SciTech Connect

The purpose of this project was to investigate and evaluate the attractiveness of using a magnesium chemical hydride slurry as a hydrogen storage, delivery, and production medium for automobiles. To fully evaluate the potential for magnesium hydride slurry to act as a carrier of hydrogen, potential slurry compositions, potential hydrogen release techniques, and the processes (and their costs) that will be used to recycle the byproducts back to a high hydrogen content slurry were evaluated. A 75% MgH2 slurry was demonstrated, which was just short of the 76% goal. This slurry is pumpable and storable for months at a time at room temperature and pressure conditions and it has the consistency of paint. Two techniques were demonstrated for reacting the slurry with water to release hydrogen. The first technique was a continuous mixing process that was tested for several hours at a time and demonstrated operation without external heat addition. Further work will be required to reduce this design to a reliable, robust system. The second technique was a semi-continuous process. It was demonstrated on a 2 kWh scale. This system operated continuously and reliably for hours at a time, including starts and stops. This process could be readily reduced to practice for commercial applications. The processes and costs associated with recycling the byproducts of the water/slurry reaction were also evaluated. This included recovering and recycling the oils of the slurry, reforming the magnesium hydroxide and magnesium oxide byproduct to magnesium metal, hydriding the magnesium metal with hydrogen to form magnesium hydride, and preparing the slurry. We found that the SOM process, under development by Boston University, offers the lowest cost alternative for producing and recycling the slurry. Using the H2A framework, a total cost of production, delivery, and distribution of $4.50/kg of hydrogen delivered or $4.50/gge was determined. Experiments performed at Boston University have demonstrated the technical viability of the process and have provided data for the cost analyses that have been performed. We also concluded that a carbothermic process could also produce magnesium at acceptable costs. The use of slurry as a medium to carry chemical hydrides has been shown during this project to offer significant advantages for storing, delivering, and distributing hydrogen: Magnesium hydride slurry is stable for months and pumpable. The oils of the slurry minimize the contact of oxygen and moisture in the air with the metal hydride in the slurry. Thus reactive chemicals, such as lithium hydride, can be handled safely in the air when encased in the oils of the slurry. Though magnesium hydride offers an additional safety feature of not reacting readily with water at room temperatures, it does react readily with water at temperatures above the boiling point of water. Thus when hydrogen is needed, the slurry and water are heated until the reaction begins, then the reaction energy provides heat for more slurry and water to be heated. The reaction system can be relatively small and light and the slurry can be stored in conventional liquid fuel tanks. When transported and stored, the conventional liquid fuel infrastructure can be used. The particular metal hydride of interest in this project, magnesium hydride, forms benign byproducts, magnesium hydroxide (Milk of Magnesia) and magnesium oxide. We have estimated that a magnesium hydride slurry system (including the mixer device and tanks) could meet the DOE 2010 energy density goals. ? During the investigation of hydriding techniques, we learned that magnesium hydride in a slurry can also be cycled in a rechargeable fashion. Thus, magnesium hydride slurry can act either as a chemical hydride storage medium or as a rechargeable hydride storage system. Hydrogen can be stored and delivered and then stored again thus significantly reducing the cost of storing and delivering hydrogen. Further evaluation and development of this concept will be performed as follow-on work under a

McClaine, Andrew W.

2008-09-30T23:59:59.000Z

215

A Continuous Solar Thermochemical Hydrogen Production Plant Design  

E-Print Network (OSTI)

Hydrogen from Solar via Light- Assisted High-TemperatureHydrogen from Solar via Light-Assisted High-Temperature

Luc, Wesley Wai

216

DOE Hydrogen Analysis Repository: H2 Production by Fermentation  

NLE Websites -- All DOE Office Websites (Extended Search)

H2 Production by Fermentation H2 Production by Fermentation Project Summary Full Title: Boundary Analysis for H2 Production by Fermentation Project ID: 70 Principal Investigator: Tim Eggeman Keywords: Hydrogen production; pressure swing adsorption (PSA); glucose; costs; fermentation Performer Principal Investigator: Tim Eggeman Organization: Neoterics International Address: 2319 S. Ellis Ct. Lakewood, CO 80228 Telephone: 303-358-6390 Email: time@NeotericsInt.com Sponsor(s) Name: Roxanne Garland Organization: DOE/EERE/HFCIT Telephone: 202-586-7260 Email: Roxanne.Garland@ee.doe.gov Name: Margaret Mann Organization: National Renewable Energy Laboratory Telephone: 303-275-2921 Email: Margaret_mann@nrel.gov Period of Performance Start: July 2001 End: September 2004 Project Description Type of Project: Analysis

217

HIGH-TEMPERATURE ELECTROLYSIS FOR HYDROGEN PRODUCTION FROM NUCLEAR ENERGY  

SciTech Connect

An experimental study is under way to assess the performance of solid-oxide cells operating in the steam electrolysis mode for hydrogen production over a temperature range of 800 to 900C. Results presented in this paper were obtained from a ten-cell planar electrolysis stack, with an active area of 64 cm2 per cell. The electrolysis cells are electrolyte-supported, with scandia-stabilized zirconia electrolytes (~140 m thick), nickel-cermet steam/hydrogen electrodes, and manganite air-side electrodes. The metallic interconnect plates are fabricated from ferritic stainless steel. The experiments were performed over a range of steam inlet mole fractions (0.1 - 0.6), gas flow rates (1000 - 4000 sccm), and current densities (0 to 0.38 A/cm2). Steam consumption rates associated with electrolysis were measured directly using inlet and outlet dewpoint instrumentation. Cell operating potentials and cell current were varied using a programmable power supply. Hydrogen production rates up to 90 Normal liters per hour were demonstrated. Values of area-specific resistance and stack internal temperatures are presented as a function of current density. Stack performance is shown to be dependent on inlet steam flow rate.

James E. O'Brien; Carl M. Stoots; J. Stephen Herring; Joseph J. Hartvigsen

2005-10-01T23:59:59.000Z

218

Overview of High-Temperature Electrolysis for Hydrogen Production  

SciTech Connect

Over the last five years there has been a growing interest in the use of hydrogen as an energy carrier, particularly to augment transportation fuels and thus reduce our dependence on imported petroleum. Hydrogen is now produced primarily via steam reforming of methane. However, in the long term, methane reforming is not a viable process for the large-scale hydrogen production since such fossil fuel conversion processes consume non-renewable resources and emit greenhouse gases. Nuclear energy can be used to produce hydrogen without consuming fossil fuels and without emitting greenhouse gases through the splitting of water into hydrogen and oxygen. The Nuclear Hydrogen Initiative of the DOE Office of Nuclear Energy is developing three general categories of high temperature processes for hydrogen production: thermochemical, electrolytic and hybrid thermo-electrolytic. This paper introduces the work being done in the development of high temperature electrolysis of steam. High Temperature Electrolysis (HTE) is built on the technology of solid oxide fuel cells (SOFCs), which were invented over a century ago, but which have been most vigorously developed during the last twenty years. SOFCs consume hydrogen and oxygen and produce steam and electricity. Solid Oxide Electrolytic Cells (SOECs) consume electricity and steam and produce hydrogen and oxygen. The purpose of the HTE research is to solve those problems unique to the electrolytic mode of operation, while building further on continuing fuel cell development. ORGANIZATION Experiments have been conducted for the last three years at the Idaho National Laboratory and at Ceramatec, Inc. on the operation of button cells and of progressively larger stacks of planar cells. In addition, the INL has been performing analyses of the cell-scale fluid dynamics and plant-scale flowsheets in order to determine optimum operating conditions and plant configurations. Argonne National Laboratory has been performing experiments for the development of new electrode materials, as well as modeling of the fluid dynamics and flowsheets for comparison with the work being done at the INL. ANL has also been performing diagnostic measures on components form long-duration tests at the INL and Ceramatec to determine the causes for the slow degradation in cell performance. Oak Ridge National Laboratory has been developing high temperature porous membranes for the separation of hydrogen from the residual steam, thus avoiding the need to condense and reheat the steam. The University of Nevada at Las Vegas has been collaborating with ANL on the development of electrode and electrolyte materials and will soon begin to investigate the causes of cell degradation. HTE research also includes NERI projects at the Virginia Polytechnic Institute on the development of toughened SOEC composite seals and at the Georgia Institute of Technology on the microstructural design of SOEC materials. EXPERIMENTAL RESULTS The most recent large-scale test of HTE was performed from June 28 through Sept 22, 2006 at the Ceramatec plant in Salt Lake City. The test apparatus consists of two stacks of 60 cells each in a configuration that will be used in the Integrated Laboratory Scale (ILS) experiment during FY-07. The ILS will contain three modules of four stacks each. The Half-Module initially produced 1.2 normal m3of H2/hour and 0.65 Nm3/hr at the end of the 2040-hour continuous test.

Herring, J. S.; O'Brien, J. E.; Stoots, C. M.; Hartvigsen, J. J.; Petri, M. C.; Carter, J. D.; Bischoff, B. L.

2007-06-01T23:59:59.000Z

219

Photoelectrochemical Hydrogen Production - DOE Hydrogen and Fuel Cells Program FY 2012 Annual Progress Report  

NLE Websites -- All DOE Office Websites (Extended Search)

9 9 FY 2012 Annual Progress Report DOE Hydrogen and Fuel Cells Program Arun Madan MVSystems, Incorporated (MVS) 500 Corporate Circle, Suite L Golden, CO 80401 Phone: (303) 271-9907 Email: ArunMadan@aol.com or amadan@mvsystemsinc.com DOE Managers HQ: Eric Miller Phone: (202) 287-5829 Email: Eric.Miller@ee.doe.gov GO: David Peterson Phone: (720) 356-1747 Email: David.Peterson@go.doe.gov Contract Number: DE-FC36-07GO17105, A00 Subcontractor: University of Hawaii at Manoa (UH), Honolulu, HI Project Start Date: September 1, 2007 Project End Date: December 31, 2012 Fiscal Year (FY) 2012 Objectives Work closely with the DOE Working Group on * Photoelectrochemical (PEC) Hydrogen Production for optimizing PEC materials and devices. Develop new PEC film materials compatible with high- *

220

Resource Analysis for Hydrogen Production - DOE Hydrogen and Fuel Cells Program FY 2012 Annual Progress Report  

NLE Websites -- All DOE Office Websites (Extended Search)

3 3 FY 2012 Annual Progress Report DOE Hydrogen and Fuel Cells Program Marc W. Melaina (Primary Contact), Michael Penev and Donna Heimiller National Renewable Energy Laboratory 15013 Denver West Parkway Golden, CO 80401 Phone: (303) 275-3836 Email: Marc.Melaina@nrel.gov DOE Manager HQ: Fred Joseck Phone: (202) 586-7932 Email: Fred.Joseck@hq.doe.gov Project Start Date: October 1, 2009 Project End Date: September 28, 2012 Fiscal Year (FY) 2012 Objectives Understand the hydrogen production requirements for a * future demand scenario Estimate low-carbon energy resources required to meet * the future scenario demand Compare resource requirements to current consumption * and projected future consumption Determine resource availability geographically and on a *

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


221

A Novel Membrane Reactor for Direct Hydrogen Production From Coal  

SciTech Connect

Gas Technology Institute has developed a novel concept of a membrane reactor closely coupled with a coal gasifier for direct extraction of hydrogen from coal-derived syngas. The objective of this project is to determine the technical and economic feasibility of this concept by screening, testing and identifying potential candidate membranes under the coal gasification conditions. The best performing membranes were selected for preliminary reactor design and cost estimate. The overall economics of hydrogen production from this new process was assessed and compared with conventional hydrogen production technologies from coal. Several proton-conducting perovskite membranes based on the formulations of BCN (BaCe{sub 0.8}Nd{sub 0.2}O{sub 3-x}), BCY (BaCe{sub 0.8}Y{sub 0.2}O{sub 3-x}), SCE (Eu-doped SrCeO{sub 3}) and SCTm (SrCe{sub 0.95}Tm{sub 0.05}O{sub 3}) were successfully tested in a new permeation unit at temperatures between 800 and 1040 C and pressures from 1 to 12 bars. The experimental data confirm that the hydrogen flux increases with increasing hydrogen partial pressure at the feed side. The highest hydrogen flux measured was 1.0 cc/min/cm{sup 2} (STP) for the SCTm membrane at 3 bars and 1040 C. The chemical stability of the perovskite membranes with respect to CO{sub 2} and H{sub 2}S can be improved by doping with Zr, as demonstrated from the TGA (Thermal Gravimetric Analysis) tests in this project. A conceptual design, using the measured hydrogen flux data and a modeling approach, for a 1000 tons-per-day (TPD) coal gasifier shows that a membrane module can be configured within a fluidized bed gasifier without a substantial increase of the gasifier dimensions. Flowsheet simulations show that the coal to hydrogen process employing the proposed membrane reactor concept can increase the hydrogen production efficiency by more than 50% compared to the conventional process. Preliminary economic analysis also shows a 30% cost reduction for the proposed membrane reactor process, assuming membrane materials meeting DOE's flux and cost target. Although this study shows that a membrane module can be configured within a fluidized bed gasifier, placing the membrane module outside the gasifier in a closely coupled way in terms of temperature and pressure can still offer the same performance advantage. This could also avoid the complicated fluid dynamics and heat transfer issues when the membrane module is installed inside the gasifier. Future work should be focused on improving the permeability and stability for the proton-conducting membranes, testing the membranes with real syngas from a gasifier and scaling up the membrane size.

Shain Doong; Estela Ong; Mike Atrosphenko; Francis Lau; Mike Roberts

2006-01-20T23:59:59.000Z

222

An Analysis of Hydrogen Production from Renewable Electricity Sources: Preprint  

NLE Websites -- All DOE Office Websites (Extended Search)

An Analysis of Hydrogen An Analysis of Hydrogen Production from Renewable Electricity Sources Preprint J.I. Levene, M.K. Mann, R. Margolis, and A. Milbrandt National Renewable Energy Laboratory Prepared for ISES 2005 Solar World Congress Orlando, Florida August 6-12, 2005 Conference Paper NREL/CP-560-37612 September 2005 NOTICE The submitted manuscript has been offered by an employee of the Midwest Research Institute (MRI), a contractor of the US Government under Contract No. DE-AC36-99GO10337. Accordingly, the US Government and MRI retain a nonexclusive royalty-free license to publish or reproduce the published form of this contribution, or allow others to do so, for US Government purposes. This report was prepared as an account of work sponsored by an agency of the United States government.

223

Enhanced Hydrogen and 1,3-Propanediol Production From Glycerol by Fermentation Using  

E-Print Network (OSTI)

ARTICLE Enhanced Hydrogen and 1,3-Propanediol Production From Glycerol by Fermentation Using Mixed value products, such as hydrogen gas and 1,3-propanediol (PD), was examined using anaerobic fermentation for hydrogen produc- tion over other methods, such as electrolytic or thermo- chemical processes

224

Current (2009) State-of-the-Art Hydrogen Production Cost Estimate  

E-Print Network (OSTI)

Current (2009) State-of-the-Art Hydrogen Production Cost Estimate Using Water Electrolysis National Cost Estimate Using Water Electrolysis To: Mr. Mark Ruth, NREL, DOE Hydrogen Systems Integration Office. For central production, the hydrogen cost is at the plant gate of an electrolysis facility with a capacity

225

Rapid hydrogen production from water using aluminum nanoclusters: A quantum molecular dynamics simulation study  

E-Print Network (OSTI)

Rapid hydrogen production from water using aluminum nanoclusters: A quantum molecular dynamics Available online 31 December 2013 Keywords: Hydrogen production Water Aluminum nanoclusters Quantum molecular dynamics simulation It is hoped that a hydrogen-on-demand generator may one day start with just

Southern California, University of

226

Production of Hydrogen Peroxide by Murine Epidermal Keratinocytes following Treatment with the Tumor Promoter 12-O-Tetradecanoylphorbol-13-acetate  

Science Journals Connector (OSTI)

...measurement of hydrogen peroxide production at the 10...biochemical methods for ROI detection...intracellular hydrogen peroxide levels...A sensitive method for the estimation of hydrogen peroxide in...nism: the production of Superoxide...

Fredika M. Robertson; Andrew J. Beavis; Tatiana M. Oberyszyn; Sean M. O'Connell; Anthea Dokidos; Debra L. Laskin; Jeffrey D. Laskin; and John J. Reiners, Jr.

1990-09-15T23:59:59.000Z

227

Fuel Cell Technologies Office: Hydrogen Production Analysis Using the H2A  

NLE Websites -- All DOE Office Websites (Extended Search)

Production Production Analysis Using the H2A v3 Model (Text Version) to someone by E-mail Share Fuel Cell Technologies Office: Hydrogen Production Analysis Using the H2A v3 Model (Text Version) on Facebook Tweet about Fuel Cell Technologies Office: Hydrogen Production Analysis Using the H2A v3 Model (Text Version) on Twitter Bookmark Fuel Cell Technologies Office: Hydrogen Production Analysis Using the H2A v3 Model (Text Version) on Google Bookmark Fuel Cell Technologies Office: Hydrogen Production Analysis Using the H2A v3 Model (Text Version) on Delicious Rank Fuel Cell Technologies Office: Hydrogen Production Analysis Using the H2A v3 Model (Text Version) on Digg Find More places to share Fuel Cell Technologies Office: Hydrogen Production Analysis Using the H2A v3 Model (Text Version) on AddThis.com...

228

Photoelectrochemical Hydrogen Production on InP Nanowire Arrays with Molybdenum Sulfide Electrocatalysts  

Science Journals Connector (OSTI)

Photoelectrochemical Hydrogen Production on InP Nanowire Arrays with Molybdenum Sulfide Electrocatalysts ... Several semiconductor nanowire systems, synthesized by different methods, have been investigated by photoelectrochemistry. ... power available from the hydrogen produced and the power supplied by an external source. ...

Lu Gao; Yingchao Cui; Jia Wang; Alessandro Cavalli; Anthony Standing; Thuy T. T. Vu; Marcel A. Verheijen; Jos E. M. Haverkort; Erik P. A. M. Bakkers; Peter H. L. Notten

2014-05-29T23:59:59.000Z

229

A Simple Method To Demonstrate the Enzymatic Production of Hydrogen from Sugar  

Science Journals Connector (OSTI)

A Simple Method To Demonstrate the Enzymatic Production of Hydrogen from Sugar ... In the experimental protocol described here, it has been demonstrated that the common sugar glucose can be used to produce hydrogen using two enzymes, glucose dehydrogenase and hydrogenase. ...

Ian Hurley; Natalie Hershlag; Jonathan Woodward

1998-10-01T23:59:59.000Z

230

Summary of Electrolytic Hydrogen Production: Milestone Completion Report  

SciTech Connect

This report provides an overview of the current state of electrolytic hydrogen production technologies and an economic analysis of the processes and systems available as of December 2003. The operating specifications of commercially available electrolyzers from five manufacturers, i.e., Stuart, Teledyne, Proton, Norsk Hydro, and Avalence, are summarized. Detailed economic analyses of three systems for which cost and economic data were available were completed. The contributions of the cost of electricity, system efficiency, and capital costs to the total cost of electrolysis are discussed.

Ivy, J.

2004-09-01T23:59:59.000Z

231

Summary of Electrolytic Hydrogen Production: Milestone Completion Report  

SciTech Connect

This report provides an overview of the current state of electrolytic hydrogen production technologies and an economic analysis of the processes and systems available as of December 2003. The operating specifications of commercially available electrolyzers from five manufacturers, i.e., Stuart, Teledyne, Proton, Norsk Hydro, and Avalence, are summarized. Detailed economic analyses of three systems for which cost and economic data were available were completed. The contributions of the cost of electricity, system efficiency, and capital costs to the total cost of electrolysis are discussed.

Ivy, J.

2004-04-01T23:59:59.000Z

232

Hydrogen production by gasification of municipal solid waste  

SciTech Connect

As fossil fuel reserves run lower and lower, and as their continued widespread use leads toward numerous environmental problems, the need for clean and sustainable energy alternatives becomes ever clearer. Hydrogen fuel holds promise as such as energy source, as it burns cleanly and can be extracted from a number of renewable materials such as municipal solid waste (MSW), which can be considered largely renewable because of its high content of paper and biomass-derived products. A computer model is being developed using ASPEN Plus flow sheeting software to simulate a process which produces hydrogen gas from MSW; the model will later be used in studying the economics of this process and is based on an actual Texaco coal gasification plant design. This paper gives an overview of the complete MSW gasification process, and describes in detail the way in which MSW is modeled by the computer as a process material. In addition, details of the gasifier unit model are described; in this unit modified MSW reacts under pressure with oxygen and steam to form a mixture of gases which include hydrogen.

Rogers, R. III

1994-05-20T23:59:59.000Z

233

The use of advanced steam reforming technology for hydrogen production  

SciTech Connect

The demand for supplementary hydrogen production in refineries is growing significantly world-wide as environmental legislation concerning cleaner gasoline and diesel fuels is introduced. The main manufacturing method is by steam reforming. The process has been developed both to reduce the capital cost and increase efficiency, reliability and ease of operation. ICI Katalco`s Leading Concept Hydrogen or LCH process continues this process of improvement by replacing the conventional fired steam reformer with a type of heat exchange reformer known as the Gas Heated Reformer or GHR. The GHR was first used in the Leading Concept Ammonia process, LCA at ICI`s manufacturing site at Severnside, England and commissioned in 1988 and later in the Leading Concept Methanol (LCM) process for methanol at Melbourne, Australia and commissioned in 1994. The development of the LCH process follows on from both LCA and LCM processes. This paper describes the development and use of the GHR in steam reforming, and shows how the GHR can be used in LCH. A comparison between the LCH process and a conventional hydrogen plant is given, showing the benefits of the LCH process in certain circumstances.

Abbishaw, J.B.; Cromarty, B.J. [ICI Katalco, Billingham (United Kingdom)

1996-12-01T23:59:59.000Z

234

A Continuous Solar Thermochemical Hydrogen Production Plant Design  

E-Print Network (OSTI)

Overview of Hydrogen and Fuel Cell Research." Energy, v.34,Quantum Boost, DOE Hydrogen and Fuel Cells Program: FY 2012Analysis. DOE Hydrogen and Fuel Cells Program, Web. 22

Luc, Wesley Wai

235

Wind Energy and Production of Hydrogen and Electricity -- Opportunities for Renewable Hydrogen: Preprint  

SciTech Connect

An assessment of options for wind/hydrogen/electricity systems at both central and distributed scales provides insight into opportunities for renewable hydrogen.

Levene, J.; Kroposki, B.; Sverdrup, G.

2006-03-01T23:59:59.000Z

236

NREL Wind to Hydrogen Project: Renewable Hydrogen Production for Energy Storage & Transportation (Presentation)  

SciTech Connect

Presentation about NREL's Wind to Hydrogen Project and producing renewable hydrogen for both energy storage and transporation, including the challenges, sustainable pathways, and analysis results.

Ramsden, T.; Harrison, K.; Steward, D.

2009-11-16T23:59:59.000Z

237

DOE Hydrogen and Fuel Cells Program Record 12024: Hydrogen Production Cost Using Low-Cost Natural Gas  

NLE Websites -- All DOE Office Websites (Extended Search)

2024 Date: September 19, 2012 2024 Date: September 19, 2012 Title: Hydrogen Production Cost Using Low-Cost Natural Gas Originator: Sara Dillich, Todd Ramsden & Marc Melaina Approved by: Sunita Satyapal Date: September 24, 2012 Item: Hydrogen produced and dispensed in distributed facilities at high-volume refueling stations using current technology and DOE's Annual Energy Outlook (AEO) 2009 projected prices for industrial natural gas result in a hydrogen levelized cost of $4.49 per gallon-gasoline-equivalent (gge) (untaxed) including compression, storage and dispensing costs. The hydrogen production portion of this cost is $2.03/gge. In comparison, current analyses using low-cost natural gas with a price of $2.00 per MMBtu can decrease the hydrogen levelized cost to $3.68 per gge (untaxed) including

238

DOE Hydrogen and Fuel Cells Program Record 5012a: Well-to-Wheels Analyses for Solar and Wind Hydrogen Production  

NLE Websites -- All DOE Office Websites (Extended Search)

DOE Hydrogen and Fuel Cells Program Record DOE Hydrogen and Fuel Cells Program Record Record #: 5012a Date: December 21, 2005 Title: Well-to-Wheels Analyses for Solar & Wind Hydrogen Production Originator: Roxanne Garland Approved by: JoAnn Milliken Date: January 6, 2006 Item: This record explains the basis for the differences between the analyses of well-to-wheels energy use and greenhouse gas emissions conducted via Argonne National Laboratory's GREET Model, cited in the U.S. Department of Energy's Solar and Wind Technologies for Hydrogen Production Report to Congress, 1 and those conducted by the National Research Council, cited in the report The Hydrogen Economy: Opportunities, Costs, Barriers, and R&D Needs. 2 Well-to-Wheels Energy Use and Greenhouse Gas Emissions - Argonne National

239

Agenda for the Derived Liquids to Hydrogen Distributed Reforming Working Group (BILIWG) Hydrogen Production Technical Team Research Review  

NLE Websites -- All DOE Office Websites (Extended Search)

& Hydrogen Production Technical Team Research Review Agenda for Tuesday, November 6, 2007 Location: BCS Incorporated, 8929 Stephens Road, Laurel, MD. 20723 410-997-7778 8:30 - 9:00 Continental Breakfast 9:00 DOE Targets, Tools and Technology o Bio-Derived Liquids to Hydrogen Distributed Reforming Targets DOE, Arlene Anderson o H2A Overview, NREL, Darlene Steward o Bio-Derived Liquids to Hydrogen Distributed Reforming Cost Analysis DTI, Brian James 10:00 Research Review o Low-Cost Hydrogen Distributed Production Systems, H2Gen, Sandy Thomas o Integrated Short Contact Time Hydrogen Generator, GE Global Research, Wei Wei o Distributed Bio-Oil Reforming, NREL, Darlene Steward o High Pressure Steam Ethanol Reforming, ANL, Romesh Kumar

240

Natural Gas Used as Feedstock for Hydrogen Production  

U.S. Energy Information Administration (EIA) Indexed Site

Used as Feedstock for Hydrogen Production Used as Feedstock for Hydrogen Production (Million Cubic Feet) Period: Annual Download Series History Download Series History Definitions, Sources & Notes Definitions, Sources & Notes Area 2008 2009 2010 2011 2012 View History U.S. 188,075 143,004 154,503 169,465 183,051 2008-2012 East Coast (PADD 1) 5,149 4,178 3,346 4,815 6,313 2008-2012 Midwest (PADD 2) 37,044 36,936 45,452 44,623 46,640 2008-2012 Gulf Coast (PADD 3) 80,291 41,049 43,170 50,968 62,829 2008-2012 Rocky Mountain (PADD 4) 12,747 11,904 12,047 12,896 12,595 2008-2012 West Coast (PADD 5) 52,844 48,937 50,488 56,163 54,674 2008-2012 - = No Data Reported; -- = Not Applicable; NA = Not Available; W = Withheld to avoid disclosure of individual company data.

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


241

ENHANCED HYDROGEN ECONOMICS VIA COPRODUCTION OF FUELS AND CARBON PRODUCTS  

SciTech Connect

This Department of Energy National Energy Technology Laboratory sponsored research effort to develop environmentally cleaner projects as a spin-off of the FutureGen project, which seeks to reduce or eliminate emissions from plants that utilize coal for power or hydrogen production. New clean coal conversion processes were designed and tested for coproducing clean pitches and cokes used in the metals industry as well as a heavy crude oil. These new processes were based on direct liquefaction and pyrolysis techniques that liberate volatile liquids from coal without the need for high pressure or on-site gaseous hydrogen. As a result of the research, a commercial scale plant for the production of synthetic foundry coke has broken ground near Wise, Virginia under the auspices of Carbonite Inc. This plant will produce foundry coke by pyrolyzing a blend of steam coal feedstocks. A second plant is planned by Quantex Energy Inc (in Texas) which will use solvent extraction to coproduce a coke residue as well as crude oil. A third plant is being actively considered for Kingsport, Tennessee, pending a favorable resolution of regulatory issues.

Kennel, Elliot B; Bhagavatula, Abhijit; Dadyburjor, Dady; Dixit, Santhoshi; Garlapalli, Ravinder; Magean, Liviu; Mukkha, Mayuri; Olajide, Olufemi A; Stiller, Alfred H; Yurchick, Christopher L

2011-03-31T23:59:59.000Z

242

Hydrogen Production from Biomass via Indirect Gasification: The Impact of NREL Process Development Unit Gasifier Correlations  

SciTech Connect

This report describes a set of updated gasifier correlations developed by NREL to predict biomass gasification products and Minimum Hydrogen Selling Price.

Kinchin, C. M.; Bain, R. L.

2009-05-01T23:59:59.000Z

243

Energy Department Invests $20 Million to Advance Hydrogen Production and Delivery Technologies  

Office of Energy Efficiency and Renewable Energy (EERE)

The Energy Department today announced $20 million for ten new research and development projects that will advance hydrogen production and delivery technologies.

244

Webinar: Critical Updates to the Hydrogen Analysis Production Model (H2A v3)  

Energy.gov (U.S. Department of Energy (DOE))

Video recording and text version of the webinar, Critical Updates to the Hydrogen Analysis Production Model (H2A v3), originally presented on February 8, 2012.

245

Critical Updates to the Hydrogen Analysis Production Model (H2A v3)  

Energy.gov (U.S. Department of Energy (DOE))

Presentation slides from the February 8, 2012, Fuel Cell Technologies Program webinar, "Critical Updates to the Hydrogen Analysis Production Model (H2A v3)".

246

Techno-Economic Boundary Analysis of Biological Pathways to Hydrogen Production (2009)  

Energy.gov (U.S. Department of Energy (DOE))

Presentation by Brian James, Strategic Analysis Inc., at the Biological Hydrogen Production Workshop held September 24-25, 2013, at the National Renewable Energy Laboratory in Golden, Colorado.

247

Hydrogen Production by Polymer Electrolyte Membrane (PEM) ElectrolysisSpotlight on Giner and Proton  

Energy.gov (U.S. Department of Energy (DOE))

Slides presented at the DOE Fuel Cell Technologies Office webinar "Hydrogen Production by Polymer Electrolyte Membrane (PEM) ElectrolysisSpotlight on Giner and Proton" on May 23, 2011.

248

Next Generation Hydrogen Station Composite Data Products: Data through Quarter 4 of 2013  

SciTech Connect

This report includes 25 composite data products (CDPs) produced for next generation hydrogen stations, with data through quarter 4 of 2013.

Sprik, S.; Kurtz, J.; Peters, M.

2014-05-01T23:59:59.000Z

249

Webinar: Hydrogen Production by Polymer Electrolyte Membrane (PEM) ElectrolysisSpotlight on Giner and Proton  

Energy.gov (U.S. Department of Energy (DOE))

Video recording of the webinar, Hydrogen Production by Polymer Electrolyte Membrane (PEM) ElectrolysisSpotlight on Giner and Proton, originally presented on May 23, 2011.

250

Hydrogen production via carbon-assisted water electrolysis at room temperature.  

E-Print Network (OSTI)

??The objective of the work was to conduct carbon-assisted water electrolysis at room temperature with reduced energy costs for hydrogen production and to improve upon (more)

Bollineni, Shilpa

2008-01-01T23:59:59.000Z

251

DOE Issues 2 Requests for Information on Low-Cost Hydrogen Production and Delivery  

Energy.gov (U.S. Department of Energy (DOE))

The US DOE's FCTO has issued two RFIs seeking feedback from the research community and relevant stakeholders about hydrogen production and hydrogen delivery RD&D activities aimed at developing technologies that can ultimately produce and deliver low-cost hydrogen.

252

Performance of Sulfur Tolerant Reforming Catalysts for Production of Hydrogen from Jet Fuel Simulants  

E-Print Network (OSTI)

,2 operated by fuel cells. Unfortunately, the lack of infrastructure, such as a network of hydrogen refueling of hydrogen sulfide (H2S), which poisons the anode in the fuel cell stack, leading to low SOFC efficiencyPerformance of Sulfur Tolerant Reforming Catalysts for Production of Hydrogen from Jet Fuel

Azad, Abdul-Majeed

253

IEA agreement on the production and utilization of hydrogen: 2000 annual report  

SciTech Connect

The 2000 annual report of the IEA Hydrogen Agreement contains an overview of the agreement, including its guiding principles, latest strategic plan, and a report from the Chairman, Mr. Neil P. Rossmeissl, U.S. Department of Energy. Overviews of the National Hydrogen Programs of nine member countries are given: Canada, Japan, Lithuania, the Netherlands, Norway, Spain, Sweden, Switzerland, and the United States. Task updates are provided on the following annexes: Annex 12 - Metal Hydrides and Carbon for Hydrogen Storage, Annex 13 - Design and Optimization of Integrated Systems, Annex 14 - Photoelectrolytic Production of Hydrogen, and, Annex 15 - Photobiological Production of Hydrogen.

Elam, Carolyn C. [National Renewable Energy Lab., Golden, CO (US)] (ed.)

2001-12-01T23:59:59.000Z

254

Hydrogen Production by PEM Electrolysis: Spotlight on Giner and Proton  

NLE Websites -- All DOE Office Websites (Extended Search)

BY BY PEM ELECTROLYSIS: SPOTLIGHT ON GINER AND PROTON US DOE WEBINAR (May 23, 2011) 2 Webinar Outline *Water Electrolysis H 2 Production Overview DOE-EERE-FCT: Eric L. Miller *Spotlight: PEM Electrolysis R&D at Giner Giner Electrochemical Systems: Monjid Hamdan *Spotlight: PEM Electrolysis R&D at Proton Proton OnSite: Kathy Ayers *Q&A 3 DOE EERE-FCT Goals and Objectives Develop technologies to produce hydrogen from clean, domestic resources at a delivered and dispensed cost of $2-$4/gge Capacity (kg/day) Distributed Central 100,000,000 100,000 50,000 10,000 1,000 10 Natural Gas Reforming Photo- electro- chemical Biological Water Electrolysis (Solar) 2015-2020 Today-2015 2020-2030 Coal Gasification (No Carbon Capture) Electrolysis Water (Grid) Coal Gasification (Carbon Capture)

255

Feasibility of Hydrogen Production from Micro Hydropower Projects in Nepal  

E-Print Network (OSTI)

The current energy crisis in Nepal clearly indicates that the future energy-demand cannot be met by traditional energy-sources. Community-based micro-hydropower operations are considered to be one of the most feasible options for energy development. However, the power plant capacity factor remains very low due to limited commercial and business opportunities. Generation of hydrogen (H2) from the unutilized power could eradicate this problem. This new energy carrier is clean, can save foreign currency and increases the energy-security. The aim of this study is to determine the potential of H2 production from excess energy of a micro-hydro project in rural Nepal using HOMER from NREL.

M. S. Zaman; A. B. Chhetri; M. S. Tango

2010-01-01T23:59:59.000Z

256

Study of hydrogen production system by using PV solar energy and PEM electrolyser in Algeria  

Science Journals Connector (OSTI)

Hydrogen fuel can be produced by using solar electric energy from photovoltaic (PV) modules for the electrolysis of water without emitting carbon dioxide or requiring fossil fuels. In this paper, an assessment of the technical potential for producing hydrogen from the PV/proton exchange membrane (PEM) electrolyser system is investigated. The present study estimates the amount of hydrogen produced by this system in six locations using hourly global solar irradiations on horizontal plane and ambient temperature. The system studied in this work is composed of 60W PV module connected with a commercial 50W PEM electrolyser via DC/DC converter equipped with a maximum power point tracking. The primary objective is to develop a mathematical model of hydrogen production system, including PV module and PEM electrolyser to analyze the system performance. The secondary aim is to compare the system performance in terms of hydrogen production at seven locations situated in different regions of Algeria. The amount of hydrogen produced is estimated at seven locations situated in different regions. In terms of hydrogen production, the results show that the southern region of Algeria (Adrar, Ghardaia, Bechar and Tamanrasset) is found to have the relatively highest hydrogen production. The total annual production of hydrogen is estimated to be around 2029m3 at these sites. The hydrogen production at various sites has been found to vary according to the solar radiation.

Djamila Ghribi; Abdellah Khelifa; Said Diaf; Maouf Belhamel

2013-01-01T23:59:59.000Z

257

Enhanced Hydrogen Production from Formic Acid by Formate Hydrogen Lyase-Overexpressing Escherichia coli Strains  

Science Journals Connector (OSTI)

...the projected decrease in fossil fuel reserves on the one hand and improvements in hydrogen fuel cell technology on the other (3). A wide range of applications of hydrogen, from cars to small devices, is anticipated...

Akihito Yoshida; Taku Nishimura; Hideo Kawaguchi; Masayuki Inui; Hideaki Yukawa

2005-11-01T23:59:59.000Z

258

Kinetics of the Reduction of Wstite by Hydrogen and Carbon Monoxide for the Chemical Looping Production of Hydrogen  

E-Print Network (OSTI)

produced could be stored, e.g. by geological sequestration, making the overall process carbon-neutral, or carbon-negative when biomass is used as fuel. In addition, the hydrogen produced during the oxidation of FexO and metallic Fe in steam can be kept... Kinetics of the reduction of wstite by hydrogen and carbon monoxide for the chemical looping production of hydrogen Wen Liu a,n, Jin Yang Lim b, Marco A. Saucedo a, Allan N. Hayhurst b, Stuart A. Scott a, J.S. Dennis b a Department of Engineering...

Liu, Wen; Lim, Jin Yang; Saucedo, Marco A.; Hayhurst, Allan N.; Scott, Stuart A.; Dennis, J. S.

2014-08-13T23:59:59.000Z

259

Conceptual design of nuclear systems for hydrogen production  

E-Print Network (OSTI)

Demand for hydrogen in the transportation energy sector is expected to keep growing in the coming decades; in the short term for refining heavy oils and in the long term for powering fuel cells. However, hydrogen cannot ...

Hohnholt, Katherine J

2006-01-01T23:59:59.000Z

260

Low-Cost Production of Hydrogen and Electricity  

Office of Energy Efficiency and Renewable Energy (EERE)

Bloom Energy is testing the potential to produce low-cost hydrogen and electricity simultaneously from natural gas.

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


261

A summary of the Third Information Exchange Meeting on the nuclear production of hydrogen  

Science Journals Connector (OSTI)

The Nuclear Energy Agency of the Organisation for Economic Co-operation and Development has organised three international exchange meetings on hydrogen production through nuclear power. The most recent meeting was held in October 2005 in Oarai, Japan, and was sponsored by the International Atomic Energy Agency. The two-and-a-half-day conference covered a full range of topics related to the nuclear production of hydrogen. Presentations were made and discussions were held on the economic prospects of a hydrogen economy and nuclear power's potential role in it, global research and development activities related to hydrogen production technologies, the coupling of hydrogen production facilities to nuclear heat sources, and basic and applied science supporting nuclear hydrogen generation. The meeting presentations are available at: http://www.nea.fr/html/science/hydro/iem3/.

Mark C. Petri; Ryutaro Hino; Isao Yamagishi

2008-01-01T23:59:59.000Z

262

Hydrogen production from the reaction of solvated electrons with benzene in water-ammonia mixtures  

SciTech Connect

Product analysis data for the reaction of the ammoniated electron with benzene-water mixtures in liquid ammonia show that the dominant product is evolved hydrogen and not 1,4-cyclohexadiene.

Dewald, R.R.; Jones, S.R.; Schwartz, B.S.

1980-11-27T23:59:59.000Z

263

Design Aspects of Hybrid Adsorbent?Membrane Reactors for Hydrogen Production  

Science Journals Connector (OSTI)

Design Aspects of Hybrid Adsorbent?Membrane Reactors for Hydrogen Production ... For hydrogen to replace fossil fuels as the fuel of choice for mobile applications, it will require the creation of a production and delivery infrastructure equivalent to those that currently exist for fossil fuels. ...

Babak Fayyaz; Aadesh Harale; Byoung-Gi Park; Paul K. T. Liu; Muhammad Sahimi; Theodore T. Tsotsis

2005-05-14T23:59:59.000Z

264

A Techno-Economic Analysis of Decentralized Electrolytic Hydrogen Production for Fuel Cell Vehicles  

E-Print Network (OSTI)

A Techno-Economic Analysis of Decentralized Electrolytic Hydrogen Production for Fuel Cell Vehicles-Economic Analysis of Decentralized Electrolytic Hydrogen Production for Fuel Cell Vehicles by Sébastien Prince options considered for future fuel cell vehicles. In this thesis, a model is developed to determine

Victoria, University of

265

System Evaluation and Economic Analysis of a HTGR Powered High-Temperature Electrolysis Hydrogen Production Plant  

SciTech Connect

A design for a commercial-scale high-temperature electrolysis (HTE) plant for hydrogen production has been developed. The HTE plant is powered by a high-temperature gas-cooled reactor (HTGR) whose configuration and operating conditions are based on the latest design parameters planned for the Next Generation Nuclear Plant (NGNP). The current HTGR reference design specifies a reactor power of 600 MWt, with a primary system pressure of 7.0 MPa, and reactor inlet and outlet fluid temperatures of 322C and 750C, respectively. The power conversion unit will be a Rankine steam cycle with a power conversion efficiency of 40%. The reference hydrogen production plant operates at a system pressure of 5.0 MPa, and utilizes a steam-sweep system to remove the excess oxygen that is evolved on the anode (oxygen) side of the electrolyzer. The overall system thermal-to-hydrogen production efficiency (based on the higher heating value of the produced hydrogen) is 40.4% at a hydrogen production rate of 1.75 kg/s and an oxygen production rate of 13.8 kg/s. An economic analysis of this plant was performed with realistic financial and cost estimating assumptions. The results of the economic analysis demonstrated that the HTE hydrogen production plant driven by a high-temperature helium-cooled nuclear power plant can deliver hydrogen at a cost of $3.67/kg of hydrogen assuming an internal rate of return, IRR, of 12% and a debt to equity ratio of 80%/20%. A second analysis shows that if the power cycle efficiency increases to 44.4%, the hydrogen production efficiency increases to 42.8% and the hydrogen and oxygen production rates are 1.85 kg/s and 14.6 kg/s respectively. At the higher power cycle efficiency and an IRR of 12% the cost of hydrogen production is $3.50/kg.

Michael G. McKellar; Edwin A. Harvego; Anastasia A. Gandrik

2010-10-01T23:59:59.000Z

266

Hydrogen production by water dissociation using ceramic membranes - annual report for FY 2010.  

SciTech Connect

The objective of this project is to develop dense ceramic membranes that can produce hydrogen via coal/coal gas-assisted water dissociation without using an external power supply or circuitry. This project grew from an effort to develop a dense ceramic membrane for separating hydrogen from gas mixtures such as those generated during coal gasification, methane partial oxidation, and water-gas shift reactions. That effort led to the development of various cermet (i.e., ceramic/metal composite) membranes that enable hydrogen production by two methods. In one method, a hydrogen transport membrane (HTM) selectively removes hydrogen from a gas mixture by transporting it through either a mixed protonic/electronic conductor or a hydrogen transport metal. In the other method, an oxygen transport membrane (OTM) generates hydrogen mixed with steam by removing oxygen that is generated through water splitting. This project focuses on the development of OTMs that efficiently produce hydrogen via the dissociation of water. Supercritical boilers offer very high-pressure steam that can be decomposed to provide pure hydrogen using OTMs. Oxygen resulting from the dissociation of steam can be used for coal gasification, enriched combustion, or synthesis gas production. Hydrogen and sequestration-ready CO{sub 2} can be produced from coal and steam by using the membrane being developed in this project. Although hydrogen can also be generated by high-temperature steam electrolysis, producing hydrogen by water splitting with a mixed-conducting membrane requires no electric power or electrical circuitry.

Balachandran, U.; Dorris, S. E.; Emerson, J. E.; Lee, T. H.; Lu, Y.; Park, C. Y.; Picciolo, J. J. (Energy Systems)

2011-03-14T23:59:59.000Z

267

Hydrogen production by water dissociation using ceramic membranes - annual report for FY 2008.  

SciTech Connect

The objective of this project is to develop dense ceramic membranes that, without using an external power supply or circuitry, can produce hydrogen via coal/coal gas-assisted water dissociation. This project grew from an effort to develop a dense ceramic membrane for separating hydrogen from gas mixtures such as those generated during coal gasification, methane partial oxidation, and water-gas shift reactions. That effort led to the development of various cermet (i.e., ceramic/metal composite) membranes that enable hydrogen production by two methods. In one method, a hydrogen transport membrane (HTM) selectively removes hydrogen from a gas mixture by transporting it through either a mixed protonic/electronic conductor or a hydrogen transport metal. In the other method, an oxygen transport membrane (OTM) generates hydrogen mixed with steam by removing oxygen that is generated through water splitting. This project focuses on the development of OTMs that efficiently produce hydrogen via the dissociation of water. Supercritical boilers offer very high-pressure steam that can be decomposed to provide pure hydrogen by means of OTMs. Oxygen resulting from the dissociation of steam can be used for coal gasification, enriched combustion, or synthesis gas production. Hydrogen and sequestration-ready CO{sub 2} can be produced from coal and steam by using the membrane being developed in this project. Although hydrogen can also be generated by high-temperature steam electrolysis, producing hydrogen by water splitting with a mixed-conducting membrane requires no electric power or electrical circuitry.

Balachandran, U.; Dorris, S. E.; Emerson, J. E.; Lee, T. H.; Lu, Y.; Park, C. Y.; Picciolo, J. J.; Energy Systems

2009-03-25T23:59:59.000Z

268

Methane Steam Reforming in Hydrogen-permeable Membrane Reactor for Pure Hydrogen Production  

Science Journals Connector (OSTI)

Steam reforming of methane over a ruthenium catalyst has been carried ... hydrogen separation from the reaction mixture, the methane conversion significantly exceeds the equilibrium value, which ... an important ...

Yasuyuki Matsumura; Jianhua Tong

2008-12-01T23:59:59.000Z

269

Hydrogen Energy Stations: Poly-Production of Electricity, Hydrogen, and Thermal Energy  

E-Print Network (OSTI)

Hydrogen and Electricity: Public-Private Partnershipand electricity demands. Foster Public-Private Partnershipand electricity demands. Foster Public-Private Partnership

Lipman, Timothy; Brooks, Cameron

2006-01-01T23:59:59.000Z

270

Sonoelectrochemical (20 khz) production of hydrogen from aqueous solutions.  

E-Print Network (OSTI)

??There are various methods of producing Hydrogen. These include electrolysis, which this work is based upon, and steam reforming; currently the most commercially viable method. (more)

Symes, Daniel

2011-01-01T23:59:59.000Z

271

Distributed Hydrogen Production from Natural Gas: Independent Review Panel Report  

Energy.gov (U.S. Department of Energy (DOE))

Independent review report on the available information concerning the technologies needed for forecourts producing 150 kg/day of hydrogen from natural gas.

272

Hydrogen Production by PEM Electrolysis: Spotlight on Giner and...  

Office of Energy Efficiency and Renewable Energy (EERE) Indexed Site

inputs for zero carbon footprint - PEM technology can be integrated with solar and wind power Cost competitive with current commercial delivered hydrogen costs - Currently...

273

Distributed Hydrogen Production from Natural Gas: Independent Review  

SciTech Connect

Independent review report on the available information concerning the technologies needed for forecourts producing 150 kg/day of hydrogen from natural gas.

Fletcher, J.; Callaghan, V.

2006-10-01T23:59:59.000Z

274

A Continuous Solar Thermochemical Hydrogen Production Plant Design  

E-Print Network (OSTI)

process powered by solar thermal energy for hydrogen21 2.5 Solar Thermal Energy and Solarproduction driven by solar thermal energy is a promising

Luc, Wesley Wai

275

Sonoelectrochemical production of hydrogen via alkaline water electrolysis.  

E-Print Network (OSTI)

??Alkaline water electrolysis is a promising technology to produce clean and pure hydrogen. This technology coupled with the ultrasound results in an enhanced rate of (more)

Hassan Zadeh, Salman

2014-01-01T23:59:59.000Z

276

Improvements and optimisation of water electrolysis for hydrogen production.  

E-Print Network (OSTI)

??[Truncated abstract] Hydrogen as an important energy carrier has wide applications and great potentials. With ever increasing energy costs and concerns with climate change associated (more)

Zeng, Kai

2012-01-01T23:59:59.000Z

277

Bioelectrocatalysis of hydrogen oxidation/production by hydrogenases  

NLE Websites -- All DOE Office Websites (Extended Search)

of hydrogen oxidationproduction by hydrogenases Source: In: Enzymatic fuel cells: From fundamentals to applications. Edited by H. Luckarift, G. Johnson and P....

278

Impact of Hydrogen Production on U.S. Energy Markets  

Energy.gov (U.S. Department of Energy (DOE)) Indexed Site

Models * A portfolio of models will be employed to project demands for hydrogen as a fuel, and impacts on feedstock price and supplies under alternative technological,...

279

Hydrogen  

Science Journals Connector (OSTI)

Hydrogen energy is a clean or inexhaustible energy like renewable energy and nuclear energy. Todays energy supply has a considerable impact on the environment. Hydrogen energy is a promising alternative solut...

2009-01-01T23:59:59.000Z

280

Economic Analysis of a Nuclear Reactor Powered High-Temperature Electrolysis Hydrogen Production Plant  

SciTech Connect

A reference design for a commercial-scale high-temperature electrolysis (HTE) plant for hydrogen production was developed to provide a basis for comparing the HTE concept with other hydrogen production concepts. The reference plant design is driven by a high-temperature helium-cooled nuclear reactor coupled to a direct Brayton power cycle. The reference design reactor power is 600 MWt, with a primary system pressure of 7.0 MPa, and reactor inlet and outlet fluid temperatures of 540C and 900C, respectively. The electrolysis unit used to produce hydrogen includes 4,009,177 cells with a per-cell active area of 225 cm2. The optimized design for the reference hydrogen production plant operates at a system pressure of 5.0 MPa, and utilizes an air-sweep system to remove the excess oxygen that is evolved on the anode (oxygen) side of the electrolyzer. The inlet air for the air-sweep system is compressed to the system operating pressure of 5.0 MPa in a four-stage compressor with intercooling. The alternating-current, AC, to direct-current, DC, conversion efficiency is 96%. The overall system thermal-to-hydrogen production efficiency (based on the lower heating value of the produced hydrogen) is 47.12% at a hydrogen production rate of 2.356 kg/s. An economic analysis of this plant was performed using the standardized H2A Analysis Methodology developed by the Department of Energy (DOE) Hydrogen Program, and using realistic financial and cost estimating assumptions. The results of the economic analysis demonstrated that the HTE hydrogen production plant driven by a high-temperature helium-cooled nuclear power plant can deliver hydrogen at a competitive cost. A cost of $3.23/kg of hydrogen was calculated assuming an internal rate of return of 10%.

E. A. Harvego; M. G. McKellar; M. S. Sohal; J. E. O'Brien; J. S. Herring

2008-08-01T23:59:59.000Z

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


281

System for the co-production of electricity and hydrogen  

DOE Patents (OSTI)

Described herein is a system for the co-generation of hydrogen gas and electricity, wherein the proportion of hydrogen to electricity can be adjusted from 0% to 100%. The system integrates fuel cell technology for power generation with fuel-assisted steam-electrolysis. A hydrocarbon fuel, a reformed hydrocarbon fuel, or a partially reformed hydrocarbon fuel can be fed into the system.

Pham, Ai Quoc (San Jose, CA); Anderson, Brian Lee (Lodi, CA)

2007-10-02T23:59:59.000Z

282

Controlled Hydrogen Fleet and Infrastructure Demonstration and Validation Project: Fall 2009; Composite Data Products, Final Version September 11, 2009  

SciTech Connect

Graphs of composite data products produced by DOE's Controlled Hydrogen Fleet and Infrastructure Demonstration and Validation project through September 2009.

Wipke, K.; Sprik, S.; Kurtz, J.; Ramsden, T.

2009-09-01T23:59:59.000Z

283

Controlled Hydrogen Fleet and Infrastructure Demonstration and Validation Project: Spring 2009; Composite Data Products, Final Version March 19, 2009  

SciTech Connect

Graphs of composite data products produced by DOE's Controlled Hydrogen Fleet and Infrastructure Demonstration and Validation project through March 2009.

Wipke, K.; Sprik, S.; Kurtz, J.; Ramsden, T.

2009-03-01T23:59:59.000Z

284

Controlled Hydrogen Fleet and Infrastructure Demonstration and Validation Project: Spring 2010; Composite Data Products, Final Version March 29, 2010  

SciTech Connect

Graphs of composite data products produced by DOE's Controlled Hydrogen Fleet and Infrastructure Demonstration and Validation project through March 2010.

Wipke, K.; Sprik, S.; Kurtz, J.; Ramsden, T.

2010-05-01T23:59:59.000Z

285

Controlled Hydrogen Fleet and Infrastructure Demonstration and Validation Project; Spring 2008 Composite Data Products, Final Version: February 29, 2008  

SciTech Connect

Graphs of composite data products produced by DOE's Controlled Hydrogen Fleet and Infrastructure Demonstration and Validation project through February 2008.

Wipke, K.; Sprik, S.; Kurtz J.

2008-04-01T23:59:59.000Z

286

Estimating Hydrogen Production Potential in Biorefineries Using Microbial Electrolysis Cell Technology  

SciTech Connect

Microbial electrolysis cells (MECs) are devices that use a hybrid biocatalysis-electrolysis process for production of hydrogen from organic matter. Future biofuel and bioproducts industries are expected to generate significant volumes of waste streams containing easily degradable organic matter. The emerging MEC technology has potential to derive added- value from these waste streams via production of hydrogen. Biorefinery process streams, particularly the stillage or distillation bottoms contain underutilized sugars as well as fermentation and pretreatment byproducts. In a lignocellulosic biorefinery designed for producing 70 million gallons of ethanol per year, up to 7200 m3/hr of hydrogen can be generated. The hydrogen can either be used as an energy source or a chemical reagent for upgrading and other reactions. The energy content of the hydrogen generated is sufficient to meet 57% of the distillation energy needs. We also report on the potential for hydrogen production in existing corn mills and sugar-based biorefineries. Removal of the organics from stillage has potential to facilitate water recycle. Pretreatment and fermentation byproducts generated in lignocellulosic biorefinery processes can accumulate to highly inhibitory levels in the process streams, if water is recycled. The byproducts of concern including sugar- and lignin- degradation products such as furans and phenolics can also be converted to hydrogen in MECs. We evaluate hydrogen production from various inhibitory byproducts generated during pretreatment of various types of biomass. Finally, the research needs for development of the MEC technology and aspects particularly relevant to the biorefineries are discussed.

Borole, Abhijeet P [ORNL; Mielenz, Jonathan R [ORNL

2011-01-01T23:59:59.000Z

287

Involvement of Hydrogen Peroxide Production in Erbstatin-induced Apoptosis in Human Small Cell Lung Carcinoma Cells  

Science Journals Connector (OSTI)

...be due to hydrogen peroxide production via newly...MATERIALS AND METHODS Materials...diaminobenzidine. This method is con 4978 Involvement of Hydrogen Peroxide Production in Erbstatin-induced...erbstatin of hydrogen peroxide production in Ms-i...oeMaterialsand Methods. For the...

Siro Simizu; Masaya Imoto; Noriyuki Masuda; Minoru Takada; and Kazuo Umezawa

1996-11-01T23:59:59.000Z

288

Production of Hydroxyl-free Radical by Reaction of Hydrogen Peroxide with N-Methyl-N?-nitro-N-nitrosoguanidine  

Science Journals Connector (OSTI)

...by reaction of hydrogen peroxide (H2O2...resulted in -OH production. INTRODUCTION...MATERIALS AND METHODS Production of -OH...formation from hydrogen peroxide by ferrous...Statistical Methods,pp. 100-106...derived from hydrogen peroxide in lignin...mechanismfor the production of ethylene from...

Tomiko Mikuni; Masaharu Tatsuta; and Mikiharu Kamachi

1985-12-01T23:59:59.000Z

289

Enhanced Hydrogen Production Integrated with CO2 Separation in a Single-Stage Reactor  

NLE Websites -- All DOE Office Websites (Extended Search)

EnhancEd hydrogEn Production EnhancEd hydrogEn Production intEgratEd with co 2 SEParation in a SinglE-StagE rEactor Description One alternative for the United States to establish independence from foreign energy sources is to utilize the nation's abundant domestic reserves of coal. Gasification provides a route to produce liquid fuels, chemical feedstocks, and hydrogen from coal. Coal continues to be viewed as the fuel source for the 21st century. Products from coal gasification, however, contain other gases, particularly carbon dioxide, as well as other contaminants that must be removed to produce the pure stream of hydrogen needed to operate fuel cells and other devices. This project seeks to demonstrate a technology to efficiently produce a pure hydrogen stream from

290

Hydrogen Pathways: Cost, Well-to-Wheels Energy Use, and Emissions for the Current Technology Status of Seven Hydrogen Production, Delivery, and Distribution Scenarios  

Energy.gov (U.S. Department of Energy (DOE))

Report of levelized cost in 2005 US dollars, energy use, and GHG emission benefits of seven hydrogen production, delivery, and distribution pathways.

291

Hydrogen Pathways: Cost, Well-to-Wheels Energy Use, and Emissions for the Current Technology Status of Seven Hydrogen Production, Delivery, and Distribution Scenarios  

Fuel Cell Technologies Publication and Product Library (EERE)

Report of levelized cost in 2005 U.S. dollars, energy use, and GHG emission benefits of seven hydrogen production, delivery, and distribution pathways.

292

Enrichment and hydrogen production by marine anaerobic hydrogen-producing microflora  

Science Journals Connector (OSTI)

Acid, alkali, heat-shock, KNO3 and control pretreatment methods applied to anaerobic sludge were evaluated for their ability to selectively enrich the marine hydrogen-producing mixed microflora. Seawater culture ...

JinLing Cai; GuangCe Wang; YanChuan Li; DaLing Zhu

2009-08-01T23:59:59.000Z

293

Hydrogen Energy Stations: Poly-Production of Electricity, Hydrogen, and Thermal Energy  

E-Print Network (OSTI)

y d r o g e n Energy Stations New York State Energy Researchin an effort led by the New York State Energy Research andNYSERDA) (2005), New York Hydrogen Energy Roadmap, NYSERDA

Lipman, Timothy; Brooks, Cameron

2006-01-01T23:59:59.000Z

294

Hydrogen Energy Stations: Poly-Production of Electricity, Hydrogen, and Thermal Energy  

E-Print Network (OSTI)

and fuel cell main- tenance and stack refurbishment costs.fuel cell stack to internally reform input fuel into hydrogen (obviating the need for a separate reformer system and reducing costs),

Lipman, Timothy; Brooks, Cameron

2006-01-01T23:59:59.000Z

295

Effect of Water Transport on the Production of Hydrogen and Sulfuric Acid in a PEM Electrolyzer  

E-Print Network (OSTI)

be developed that provides efficient production of clean hydrogen. The methods existing today for large-scale produc- tion of hydrogen typically involve hydrocarbon reforming of natural gas or coal gasification% , the overall efficiency is 40%.7 Two issues remain, however, that make the future of this technology un

Weidner, John W.

296

DOE NSF Partnership to Address Critical Challenges in Hydrogen Production from Solar Water Splitting  

Energy.gov (U.S. Department of Energy (DOE))

EERE and the National Science Foundation (NSF) announce a funding opportunity in the area of renewable hydrogen technology research and development, specifically addressing discovery and development of advanced materials systems and chemical proceesses for direct photochemical and/or thermochemical water splitting for application in the solar production of hydrogen fuel.

297

Production of Hydrogen and Electricity from Coal with CO2 Capture  

E-Print Network (OSTI)

fuels · H2 (and CO2) distribution · H2 utilization (e.g. fuel cells, combustion) · Princeton energy carriers are needed: electricity and hydrogen. · If CO2 sequestration is viable, fossil fuel1 Production of Hydrogen and Electricity from Coal with CO2 Capture Princeton University: Tom

298

Hydrogen Energy Stations: Poly-Production of Electricity, Hydrogen, and Thermal Energy  

E-Print Network (OSTI)

27. Keenan, G. (2006), Air Products and Chemicals Inc. ,originally devel- oped by Air Products and Chemicals, Inc. (agreement between Air Products and Chemicals Inc. and the

Lipman, Timothy; Brooks, Cameron

2006-01-01T23:59:59.000Z

299

Production of hydrogen from water using biophotolytic methods  

Science Journals Connector (OSTI)

Hydrogen gas has been produced on a continuous basis using two immobilized microorganisms. One organism, the cyanobacteria it(Anacystis nidulans), oxidizes water, producing molecular oxygen, and reduces exogen...

Howard H. Weetall; Lester O. Krampitz

1980-06-01T23:59:59.000Z

300

Biological Production of Hydrogen DOE Office of Science,  

E-Print Network (OSTI)

Research John Houghton 6/2/03: DOE Hydrogen and Fuel Cells Coordination Meeting 301-903-8288 John Communities Applications: Algae Ponds Source: Frank Dazzo, Center for Microbial Ecology, Michigan State

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


301

Hydrogen peroxide production by water electrolysis: Application to disinfection  

Science Journals Connector (OSTI)

Hydrogen peroxide was produced by direct current electrolysis using only two electrodes, a carbon felt...2...coated titanium anode. The required oxygen was supplied by oxidation of water and by transfer from the ...

P. Drogui; S. Elmaleh; M. Rumeau; C. Bernard

2001-08-01T23:59:59.000Z

302

Analysis of Improved Reference Design for a Nuclear-Driven High Temperature Electrolysis Hydrogen Production Plant  

SciTech Connect

The use of High Temperature Electrolysis (HTE) for the efficient production of hydrogen without the greenhouse gas emissions associated with conventional fossil-fuel hydrogen production techniques has been under investigation at the Idaho National Engineering Laboratory (INL) for the last several years. The activities at the INL have included the development, testing and analysis of large numbers of solid oxide electrolysis cells, and the analyses of potential plant designs for large scale production of hydrogen using an advanced Very-High Temperature Reactor (VHTR) to provide the process heat and electricity to drive the electrolysis process. The results of these system analyses, using the UniSim process analysis software, have shown that the HTE process, when coupled to a VHTR capable of operating at reactor outlet temperatures of 800 C to 950 C, has the potential to produce the large quantities of hydrogen needed to meet future energy and transportation needs with hydrogen production efficiencies in excess of 50%. In addition, economic analyses performed on the INL reference plant design, optimized to maximize the hydrogen production rate for a 600 MWt VHTR, have shown that a large nuclear-driven HTE hydrogen production plant can to be economically competitive with conventional hydrogen production processes, particularly when the penalties associated with greenhouse gas emissions are considered. The results of this research led to the selection in 2009 of HTE as the preferred concept in the U.S. Department of Energy (DOE) hydrogen technology down-selection process. However, the down-selection process, along with continued technical assessments at the INL, has resulted in a number of proposed modifications and refinements to improve the original INL reference HTE design. These modifications include changes in plant configuration, operating conditions and individual component designs. This paper describes the resulting new INL reference design and presents results of system analyses performed to optimize the design and to determine required plant performance and operating conditions.

Edwin A. Harvego; James E. O'Brien; Michael G. McKellar

2010-06-01T23:59:59.000Z

303

Comparing air quality impacts of hydrogen and gasoline  

E-Print Network (OSTI)

pathway, with hydrogen production at refueling stations (with centralized hydrogen production and gaseous hydrogenwith centralized hydrogen production and liquid hydrogen (

Sperling, Dan; Wang, Guihua; Ogden, Joan M.

2008-01-01T23:59:59.000Z

304

Hydrogen production with nickel powder cathode catalysts in microbial electrolysis cells  

E-Print Network (OSTI)

gasification that rely on non-renewable energy sources [1]. Electrohydrogenesis using microbial electrolysis cells (MEC) is a promising approach for hydrogen production from organic matter, including waste- water

305

Amorphous Si Thin Film Based Photocathodes with High Photovoltage for Efficient Hydrogen Production  

E-Print Network (OSTI)

of California, Berkeley, California 94720, United States Joint Center for Artificial Photosynthesis and § Materials Sciences Division, Lawrence Berkeley National Laboratory, Berkeley, California 94720, United for solar hydrogen production. With platinum as prototypical cocatalyst, a photocurrent onset potential of 0

Javey, Ali

306

DOE Fuel Cell Technologies Office Record 12024: Hydrogen Production Cost Using Low-Cost Natural Gas  

Energy.gov (U.S. Department of Energy (DOE))

This program record from the U.S. Department of Energy's Fuel Cell Technologies Office provides information about the cost of hydrogen production using low-cost natural gas.

307

Solar Thermochemical Hydrogen Production Research (STCH): Thermochemical Cycle Selection and Investment Priority  

Energy.gov (U.S. Department of Energy (DOE))

This Sandia National Laboratories report documents the evaluation of nine solar thermochemical reaction cycles for the production of hydrogen and identifies the critical path challenges to the commercial potential of each cycle.

308

A resource recycling technique of hydrogen production from the catalytic degradation of organics in wastewater  

Science Journals Connector (OSTI)

A resource recycling technique of hydrogen production from the catalytic degradation of organics in wastewater by aqueous phase reforming (APR) has...N,N-dimethylformamide (DMF) and cyclohexanol) in water could b...

XiaoNian Li; LingNiao Kong; YiZhi Xiang; YaoMing Ju

2008-11-01T23:59:59.000Z

309

Microbial Electrolysis Cells (MECs) for High Yield Hydrogen (H2) Production from Biodegradable Materials  

Energy.gov (U.S. Department of Energy (DOE))

Presentation by Jason Ren, University of Colorado Boulder, at the Biological Hydrogen Production Workshop held September 24-25, 2013, at the National Renewable Energy Laboratory in Golden, Colorado.

310

DOE Issues 2 Requests for Information on Low-Cost Hydrogen Production...  

Office of Energy Efficiency and Renewable Energy (EERE) Indexed Site

on the RD&D needs for enabling low-cost, effective hydrogen production from all types of water electrolysis systems, both centralized and forecourt. Based on the results of these...

311

Liquid composition having ammonia borane and decomposing to form hydrogen and liquid reaction product  

DOE Patents (OSTI)

Liquid compositions of ammonia borane and a suitably chosen amine borane material were prepared and subjected to conditions suitable for their thermal decomposition in a closed system that resulted in hydrogen and a liquid reaction product.

Davis, Benjamin L; Rekken, Brian D

2014-04-01T23:59:59.000Z

312

Structure of aluminum hydroxide powders obtained as a byproduct of hydrogen fuel production  

Science Journals Connector (OSTI)

The structure of aluminum hydroxide powders obtained as byproducts of hydrogen fuel production was investigated. One of the main initial components comprised aluminum-magnesium chips with 0.6, 6 and 12 wt.% ma...

A. D. Shlyapin; A. Yu. Omarov; V. P. Tarasovskii; Yu. G. Trifonov

2013-09-01T23:59:59.000Z

313

Life Cycle Assessment of Hydrogen Production via Natural Gas Steam Reforming  

Energy.gov (U.S. Department of Energy (DOE))

A life cycle assessment of hydrogen production via natural gas steam reforming was performed to examine the net emissions of greenhouse gases as well as other major environmental consequences.

314

? Particles Initiate Biological Production of Superoxide Anions and Hydrogen Peroxide in Human Cells  

Science Journals Connector (OSTI)

...induce the cellular production of O2@ and H2O2 by...that the intracel lular production of O2@ and H202 is...18). MATERIALS AND METHODS Reagents. Cells were...concentration, 10 .LM).Hydrogen peroxide (H2O2; 30...intracellular O2@ and H202 production in human cells (19...

P. K. Narayanan; E. H. Goodwin; and B. E. Lehnert

1997-09-15T23:59:59.000Z

315

Production of Hydrogen Gas from Light and the Inorganic Electron Donor Thiosulfate by Rhodopseudomonas palustris  

Science Journals Connector (OSTI)

...control rates of H2 production. The possibility...compounds for H2 production by PNSBs beyond...with hydrogen fuel cells because it has a...potential for H2 production because they can...water along with solar energy to drive...studies with PNSBs, organic compounds are typically...

Jean J. Huang; Erin K. Heiniger; James B. McKinlay; Caroline S. Harwood

2010-10-01T23:59:59.000Z

316

Hydrogen and electricity production using microbial fuel cell-based technologies  

E-Print Network (OSTI)

1 Hydrogen and electricity production using microbial fuel cell-based technologies Bruce E. Logan/mol? ? #12;8 Energy Production using MFC technologies · Electricity production using microbial fuel cells · H to renewable energy #12;9 Demonstration of a Microbial Fuel Cell (MFC) MFC webcam (live video of an MFC running

Lee, Dongwon

317

Hydrogen production during processing of radioactive sludge containing noble metals  

SciTech Connect

Hydrogen was produced when radioactive sludge from Savannah River Site radioactive waste containing noble metals was reacted with formic acid. This will occur in a process tank in the Defense Waste Facility at SRS when waste is vitrified. Radioactive sludges from four tanks were tested in a lab-scale apparatus. Maximum hydrogen generation rates varied from 5 {times}10{sup {minus}7} g H{sub 2}/hr/g of sludge from the least reactive sludge (from Waste Tank 51) to 2 {times}10{sup {minus}4} g H{sub 2}/hr/g of sludge from the most reactive sludge (from Waste Tank 11). The time required for the hydrogen generation to reach a maximum varied from 4.1 to 25 hours. In addition to hydrogen, carbon dioxide and nitrous oxide were produced and the pH of the reaction slurry increased. In all cases, the carbon dioxide and nitrous oxide were generated before the hydrogen. The results are in agreement with large-scale studies using simulated sludges.

Ha, B.C.; Ferrara, D.M.; Bibler, N.E.

1992-09-01T23:59:59.000Z

318

Hydrogen production during processing of radioactive sludge containing noble metals  

SciTech Connect

Hydrogen was produced when radioactive sludge from Savannah River Site radioactive waste containing noble metals was reacted with formic acid. This will occur in a process tank in the Defense Waste Facility at SRS when waste is vitrified. Radioactive sludges from four tanks were tested in a lab-scale apparatus. Maximum hydrogen generation rates varied from 5 {times}10{sup {minus}7} g H{sub 2}/hr/g of sludge from the least reactive sludge (from Waste Tank 51) to 2 {times}10{sup {minus}4} g H{sub 2}/hr/g of sludge from the most reactive sludge (from Waste Tank 11). The time required for the hydrogen generation to reach a maximum varied from 4.1 to 25 hours. In addition to hydrogen, carbon dioxide and nitrous oxide were produced and the pH of the reaction slurry increased. In all cases, the carbon dioxide and nitrous oxide were generated before the hydrogen. The results are in agreement with large-scale studies using simulated sludges.

Ha, B.C.; Ferrara, D.M.; Bibler, N.E.

1992-01-01T23:59:59.000Z

319

Hydrogen and elemental carbon production from natural gas and other hydrocarbons  

DOE Patents (OSTI)

Diatomic hydrogen and unsaturated hydrocarbons are produced as reactor gases in a fast quench reactor. During the fast quench, the unsaturated hydrocarbons are further decomposed by reheating the reactor gases. More diatomic hydrogen is produced, along with elemental carbon. Other gas may be added at different stages in the process to form a desired end product and prevent back reactions. The product is a substantially clean-burning hydrogen fuel that leaves no greenhouse gas emissions, and elemental carbon that may be used in powder form as a commodity for several processes.

Detering, Brent A. (Idaho Falls, ID); Kong, Peter C. (Idaho Falls, ID)

2002-01-01T23:59:59.000Z

320

Int. J. Nuclear Hydrogen Production and Application, Vol. 1, No. 1, 2006 57 Copyright 2006 Inderscience Enterprises Ltd.  

E-Print Network (OSTI)

Int. J. Nuclear Hydrogen Production and Application, Vol. 1, No. 1, 2006 57 Copyright © 2006. (2006) `Global environmental impacts of the hydrogen economy', Int. J. Nuclear Hydrogen Production Manning is Head of the Atmospheric Dispersion Group at the UK Met Office. He holds a PhD in Experimental

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


321

Gastric Secretion: Mechanism for Production of Hydrogen Ions  

Science Journals Connector (OSTI)

...from the hydro-lytic treatment of collective carotenoids...dissociation con-stant of water and other weak elec-trolytes...electro-lyte can be water, to produce hydrogen...under conditions of electrodialysis. These studies were...electric field, of either water or carbonic acid at...

Harry P. Gregor; Jesse M. Berkowitz

1965-11-05T23:59:59.000Z

322

Engineering a Synthetic Dual-Organism System for Hydrogen Production  

Science Journals Connector (OSTI)

...promising renewable energy source as pressure...but they are also energy intensive and therefore...due to its use of renewable biomass or sunlight as its primary energy source. Hydrogen...due to the current cost of its chemical synthesis...

Zeev Waks; Pamela A. Silver

2009-02-06T23:59:59.000Z

323

Optimization of membrane stack configuration for efficient hydrogen production in microbial reverse-electrodialysis electrolysis cells coupled  

E-Print Network (OSTI)

Optimization of membrane stack configuration for efficient hydrogen production in microbial reverse-electrodialysis 2013 Keywords: Microbial reverse-electrodialysis electrolysis cell Ammonium bicarbonate Hydrogen reverse electrodialysis (RED) stack into the MEC, which was called a microbial reverse-electrodialysis

324

Hydrogen production by water dissociation using ceramic membranes. Annual report for FY 2007.  

SciTech Connect

The objective of this project is to develop dense ceramic membranes that, without using an external power supply or circuitry, can produce hydrogen via coal/coal gas-assisted water dissociation. This project grew out of an effort to develop a dense ceramic membrane for separating hydrogen from gas mixtures such as those generated during coal gasification, methane partial oxidation, and water-gas shift reactions [1]. That effort led to the development of various cermet (i.e., ceramic/metal composite) membranes that enable hydrogen to be produced by two methods. In one method, a hydrogen transport membrane (HTM) selectively removes hydrogen from a gas mixture by transporting it through either a mixed protonic/electronic conductor or a hydrogen transport metal. In the other method, an oxygen transport membrane (OTM) generates hydrogen mixed with steam by removing oxygen that is generated through water splitting [1, 2]. This project focuses on the development of OTMs that efficiently produce hydrogen via the dissociation of water. Supercritical boilers offer very high-pressure steam that can be decomposed to provide pure hydrogen by means of OTMs. Oxygen resulting from the dissociation of steam can be used for coal gasification, enriched combustion, or synthesis gas production. Hydrogen and sequestration-ready CO{sub 2} can be produced from coal and steam by using the membrane being developed in this project. Although hydrogen can also be generated by high-temperature steam electrolysis, producing hydrogen by water splitting with a mixed-conducting membrane requires no electric power or electrical circuitry.

Balachandran, U.; Chen, L.; Dorris, S. E.; Emerson, J. E.; Lee, T. H.; Park, C. Y.; Picciolo, J. J.; Song, S. J.; Energy Systems

2008-03-04T23:59:59.000Z

325

Process modeling of hydrogen production from municipal solid waste  

SciTech Connect

The ASPEN PLUS commercial simulation software has been used to develop a process model for a conceptual process to convert municipal solid waste (MSW) to hydrogen. The process consists of hydrothermal treatment of the MSW in water to create a slurry suitable as feedstock for an oxygen blown Texaco gasifier. A method of reducing the complicated MSW feed material to a manageable set of components is outlined along with a framework for modeling the stoichiometric changes associated with the hydrothermal treatment process. Model results indicate that 0.672 kmol/s of hydrogen can be produced from the processing of 30 kg/s (2600 tonne/day) of raw MSW. A number of variations on the basic processing parameters are explored and indicate that there is a clear incentive to reduce the inert fraction in the processed slurry feed and that cofeeding a low value heavy oil may be economically attractive.

Thorsness, C.B.

1995-01-01T23:59:59.000Z

326

Hydrogen production and delivery analysis in US markets : cost, energy and greenhouse gas emissions.  

SciTech Connect

Hydrogen production cost conclusions are: (1) Steam Methane Reforming (SMR) is the least-cost production option at current natural gas prices and for initial hydrogen vehicle penetration rates, at high production rates, SMR may not be the least-cost option; (2) Unlike coal and nuclear technologies, the cost of natural gas feedstock is the largest contributor to SMR production cost; (3) Coal- and nuclear-based hydrogen production have significant penalties at small production rates (and benefits at large rates); (4) Nuclear production of hydrogen is likely to have large economies of scale, but because fixed O&M costs are uncertain, the magnitude of these effects may be understated; and (5) Given H2A default assumptions for fuel prices, process efficiencies and labor costs, nuclear-based hydrogen is likely to be more expensive to produce than coal-based hydrogen. Carbon taxes and caps can narrow the gap. Hydrogen delivery cost conclusions are: (1) For smaller urban markets, compressed gas delivery appears most economic, although cost inputs for high-pressure gas trucks are uncertain; (2) For larger urban markets, pipeline delivery is least costly; (3) Distance from hydrogen production plant to city gate may change relative costs (all results shown assume 100 km); (4) Pipeline costs may be reduced with system 'rationalization', primarily reductions in service pipeline mileage; and (5) Liquefier and pipeline capital costs are a hurdle, particularly at small market sizes. Some energy and greenhouse gas Observations: (1) Energy use (per kg of H2) declines slightly with increasing production or delivery rate for most components (unless energy efficiency varies appreciably with scale, e.g., liquefaction); (2) Energy use is a strong function of production technology and delivery mode; (3) GHG emissions reflect the energy efficiency and carbon content of each component in a production-delivery pathway; (4) Coal and natural gas production pathways have high energy consumption and significant GHG emissions (in the absence of carbon caps, taxes or sequestration); (5) Nuclear pathway is most favorable from energy use and GHG emissions perspective; (6) GH2 Truck and Pipeline delivery have much lower energy use and GHG emissions than LH2 Truck delivery; and (7) For LH2 Truck delivery, the liquefier accounts for most of the energy and GHG emissions.

Mintz, M.; Gillette, J.; Elgowainy, A. (Decision and Information Sciences); ( ES)

2009-01-01T23:59:59.000Z

327

Thermocatalytic process for CO.sub.2-free production of hydrogen and carbon from hydrocarbons  

DOE Patents (OSTI)

A novel process and apparatus are disclosed for sustainable CO.sub.2-free production of hydrogen and carbon by thermocatalytic decomposition (dissociation, pyrolysis, cracking) of hydrocarbon fuels over carbon-based catalysts in the absence of air and/or water. The apparatus and thermocatalytic process improve the activity and stability of carbon catalysts during the thermocatalytic process and produce both high purity hydrogen (at least, 99.0 volume %) and carbon, from any hydrocarbon fuel, including sulfurous fuels. In a preferred embodiment, production of hydrogen and carbon is achieved by both internal and external activation of carbon catalysts. Internal activation of carbon catalyst is accomplished by recycling of hydrogen-depleted gas containing unsaturated and aromatic hydrocarbons back to the reactor. External activation of the catalyst can be achieved via surface gasification with hot combustion gases during catalyst heating. The process and apparatus can be conveniently integrated with any type of fuel cell to generate electricity.

Muradov, Nazim Z. (Melbourne, FL)

2011-08-23T23:59:59.000Z

328

Hydrogen production from cellulose in a two-stage process combining fermentation and electrohydrogenesis  

E-Print Network (OSTI)

Hydrogen production from cellulose in a two-stage process combining fermentation primarily of: acetic, lactic, succinic, and formic acids and ethanol. An additional 800 ? 290 mL H2/g #12;1. Introduction Biohydrogen production from cellulose has received consid- erable attention

329

Designing catalysts for hydrogen production | Center for Bio...  

NLE Websites -- All DOE Office Websites (Extended Search)

production 12 Oct 2012 Dr. Anne Jones is a Principal Investigator in the Center of Bio-Inspired Solar Fuel production at Arizona State University. Her lab is involved in...

330

Intracellular Hydrogen Peroxide Production Is an Upstream Event in Apoptosis Induced by Down-Regulation of Casein Kinase 2 in Prostate Cancer Cells  

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...hydrogen peroxide production independent of the...Kundu GC, et al. Hydrogen peroxide activates...S, Clement MV. Hydrogen peroxide-induced...reductive stress. Methods Enzymol 2002;352...Increased Nox1 and hydrogen peroxide in prostate...hydrogen peroxide production is an upstream event...

Kashif A. Ahmad; Guixia Wang; and Khalil Ahmed

2006-05-01T23:59:59.000Z

331

Enhanced Hydrogen Production Integrated with CO2 Separation in a Single-Stage Reactor  

SciTech Connect

High purity hydrogen is commercially produced from syngas by the Water Gas Shift Reaction (WGSR) in high and low temperature shift reactors using iron oxide and copper catalysts respectively. However, the WGSR is thermodynamically limited at high temperatures towards hydrogen production necessitating excess steam addition and catalytic operation. In the calcium looping process, the equilibrium limited WGSR is driven forward by the incessant removal of CO{sub 2} by-product through the carbonation of calcium oxide. At high pressures, this process obviates the need for a catalyst and excess steam requirement, thereby removing the costs related to the procurement and deactivation of the catalyst and steam generation. Thermodynamic analysis for the combined WGS and carbonation reaction was conducted. The combined WGS and carbonation reaction was investigated at varying pressures, temperatures and S/C ratios using a bench scale reactor system. It was found that the purity of hydrogen increases with the increase in pressure and at a pressure of 300 psig, almost 100% hydrogen is produced. It was also found that at high pressures, high purity hydrogen can be produced using stoichiometric quantities of steam. On comparing the catalytic and non catalytic modes of operation in the presence of calcium oxide, it was found that there was no difference in the purity of hydrogen produced at elevated pressures. Multicyclic reaction and regeneration experiments were also conducted and it was found that the purity of hydrogen remains almost constant after a few cycles.

Shwetha Ramkumar; Mahesh Iyer; Danny Wong; Himanshu Gupta; Bartev Sakadjian; Liang-Lhih Fan

2008-09-30T23:59:59.000Z

332

Production of Hydrogen Using Nanocrystalline Protein-Templated Catalysts on M13 Phage  

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Production of Hydrogen Using Nanocrystalline Protein-Templated Catalysts on M13 Phage ... (35-38) In this work, we template nickel, rhodium, and ceria onto the surface of the M13 bacteriophage in order to produce catalysts with excellent dispersion, higher thermal stability, and a more porous structure than catalysts made using other methods. ... This result indicates that the selectivity to methane was partially controlled by the availability of hydrogen atoms on the surface required to hydrogenate the hydrocarbon species produced by acetaldehyde decarbonylation. ...

Brian Neltner; Brian Peddie; Alex Xu; William Doenlen; Keith Durand; Dong Soo Yun; Scott Speakman; Andrew Peterson; Angela Belcher

2010-06-07T23:59:59.000Z

333

Reversible Electrocatalytic Production and Oxidation of Hydrogen at Low Overpotentials by a Functional Hydrogenase Mimic  

SciTech Connect

A new bis(diphosphine) nickel(II) complex, [Ni(PPh2NR2)2](BF4)2, 1, (R = CH2CH2OCH3) is described. A {Delta}G{sup o} of 0.84 kcal/mol{sup -1} for hydrogen addition for this complex was calculated from the experimentally determined equilibrium constant. This complex displays reversible electrocatalytic activity for hydrogen production and oxidation at low overpotentials, a characteristic most commonly associated with hydrogenase enzymes.

Smith, Stuart E.; Yang, Jenny Y.; DuBois, Daniel L.; Bullock, Morris

2012-03-26T23:59:59.000Z

334

Development of Hydrogen Selective Membranes/Modules as Reactors/Separators for Distributed Hydrogen Production - DOE Hydrogen and Fuel Cells Program FY 2012 Annual Progress Report  

NLE Websites -- All DOE Office Websites (Extended Search)

3 3 FY 2012 Annual Progress Report DOE Hydrogen and Fuel Cells Program Paul KT Liu Media and Process Technology Inc. (M&P) 1155 William Pitt Way Pittsburgh, PA 15238 Phone: (412) 826-3711 Email: pliu@mediaandprocess.com DOE Managers HQ: Sara Dillich Phone: (202) 586-7925 Email: Sara.Dillich@ee.doe.gov GO: Katie Randolph Phone: (720) 356-1759 Email: Katie.Randolph@go.doe.gov Contract Number: DE-FG36-05GO15092 Subcontractor: University of Southern California Project Start Date: July 1, 2005 Projected End Date: December 31, 2012 Fiscal Year (FY) 2012 Objectives The water-gas shift (WGS) reaction becomes less efficient when high CO conversion is required, such as for distributed hydrogen production applications. Our project

335

Potential for Hydrogen Production from Key Renewable Resources in the United States  

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Potential for Hydrogen Production Potential for Hydrogen Production from Key Renewable Resources in the United States A. Milbrandt and M. Mann Technical Report NREL/TP-640-41134 February 2007 NREL is operated by Midwest Research Institute ● Battelle Contract No. DE-AC36-99-GO10337 Potential for Hydrogen Production from Key Renewable Resources in the United States A. Milbrandt and M. Mann Prepared under Task No. H278.2100 Technical Report NREL/TP-640-41134 February 2007 National Renewable Energy Laboratory 1617 Cole Boulevard, Golden, Colorado 80401-3393 303-275-3000 * www.nrel.gov Operated for the U.S. Department of Energy Office of Energy Efficiency and Renewable Energy by Midwest Research Institute * Battelle Contract No. DE-AC36-99-GO10337 NOTICE This report was prepared as an account of work sponsored by an agency of the United States government.

336

Experimental Study of Solar Hydrogen Production Performance by Water Electrolysis in the South of Algeria  

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Current environment problems require the uses of clean process and durable sources in industrial activities. Hydrogen, produced by water electrolysis, represents high clean energy source. In this process, a high electrical energy rate is needed which led to costly product. In order to remedy this issue, the uses of renewable energies are required. In this work, an experimental study of solar hydrogen production system by alkaline water electrolysis in Ouargla (Algeria) city is presented. The alkaline water electrolysis, with different NaOH concentrations, is feed by photovoltaic panels. The system is tested at different input conditions of voltages and currents. Effects of temperature and NaOH electrolyte concentration on hydrogen production are examined

N. Chennouf; N. Settou; B. Negrou; K. Bouziane; B. Dokkar

2012-01-01T23:59:59.000Z

337

MEASUREMENT AND PREDICTION OF RADIOLYTIC HYDROGEN PRODUCTION IN DEFENSE WASTE PROCESSING SLURRIES AT SAVANNAH RIVER SITE  

SciTech Connect

This paper presents results of measurements and predictions of radiolytic hydrogen production rates from two actual process slurries in the Defense Waste Processing Facility (DWPF) at Savannah River Site (SRS). Hydrogen is a flammable gas and its production in nuclear facilities can be a safety hazard if not mitigated. Measurements were made in the Shielded Cells of Savannah River National Laboratory (SRNL) using a sample of Sludge Batch 3 (SB3) currently being processed by the DWPF. Predictions were made using published values for rates of radiolytic reactions producing H{sub 2} in aqueous solutions and the measured radionuclide and chemical compositions of the two slurries. The agreement between measured and predicted results for nine experiments ranged from complete agreement to 24% difference. This agreement indicates that if the composition of the slurry being processed is known, the rate of radiolytic hydrogen production can be reasonably estimated.

Bibler, N; John Pareizs, J; Terri Fellinger, T; Cj Bannochie, C

2007-01-10T23:59:59.000Z

338

Photocatalytic Hydrogen Production from Noncovalent Biohybrid Photosystem I/Pt Nanoparticle Complexes  

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Photocatalytic Hydrogen Production from Noncovalent Biohybrid Photosystem I/Pt Nanoparticle Complexes ... (11) The PSI/Pt nanoparticle system described here, with a soluble donor, reproducibly produces H2 at the same order of magnitude as the fully optimized PSI/molecular wire/Pt nanoparticle system and potentially could produce even higher rates of H2 with a cross-linked donor. ... Experimental methods for sample preparation, H2 production studies, EPR measurements, and video of H2 production. ...

Lisa M. Utschig; Nada M. Dimitrijevic; Oleg G. Poluektov; Sergey D. Chemerisov; Karen L. Mulfort; David M. Tiede

2011-01-19T23:59:59.000Z

339

Novel methods of hydrogen production: aluminum-gallium-indium-tin systems and copper boron oxide as photocatalysts.  

E-Print Network (OSTI)

??In recent years, hydrogen production and storage has attracted a lot of attention in both academia and industry due to its variety of applications in (more)

Lang, Yizhao

2011-01-01T23:59:59.000Z

340

Controlled Hydrogen Fleet and Infrastructure Demonstration and Validation Project: Spring 2007 Composite Data Products; March 8, 2007  

SciTech Connect

This presentation provides the composite data products from Spring 2007 from NREL's Controlled Hydrogen Fleet and Infrastructure Demonstration and Validation Project.

Wipke, K.; Sprik, S.; Thomas, H.; Welch, C.

2007-04-01T23:59:59.000Z

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
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to obtain the most current and comprehensive results.


341

Requirements for low cost electricity and hydrogen fuel production from multi-unit intertial fusion energy plants with a shared driver and target factory  

E-Print Network (OSTI)

hydrogen fuel by electrolysis meeting equal consumer costhydrogen fuel production by water electrolysis to provide lower fuel costFig. 2: Cost hydrogen bywater of (Coil) electrolysis as

Logan, B. Grant; Moir, Ralph; Hoffman, Myron A.

1994-01-01T23:59:59.000Z

342

Catalysis Letters Vol. 72, No. 3-4, 2001 197 Catalytic ammonia decomposition: COx-free hydrogen production  

E-Print Network (OSTI)

as a method to produce hydrogen for fuel cell applications. The absence of any undesirable by-products (unlike of hydrogen for fuel cells. In this study a variety of supported metal catalysts have been studied. Supported is the recent interest in the generation of clean hydrogen for fuel cells. Conventional processes such as steam

Goodman, Wayne

343

Chemical Engineering Journal 93 (2003) 6980 Production of COx-free hydrogen for fuel cells via step-wise hydrocarbon  

E-Print Network (OSTI)

Chemical Engineering Journal 93 (2003) 69­80 Production of COx-free hydrogen for fuel cells via Abstract The stringent COx-free hydrogen requirement for the current low temperature fuel cells has Hydrogen is the most promising fuel for the low temper- ature fuel cells, however, chemical processes

Goodman, Wayne

344

DOE Hydrogen Analysis Repository: Water Implications of Biofuels Production  

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Water Implications of Biofuels Production Water Implications of Biofuels Production Project Summary Full Title: Water Implications of Biofuels Production in the United States Project ID: 227 Principal Investigator: William S. Logan Brief Description: The National Research Council conducted a workshop and wrote a report examining the potential effects of biofuels production in the U.S. on water and related land resources. Purpose Examine the possible effects of biofuel development on water and related land resources. The central questions are how water use and water quality are expected to change as the U.S. agricultural portfolio shifts to include more energy crops and as overall agricultural production potentially increases. Such questions are considered within the context of U.S. policy and also the expected advances in technology and agricultural practices

345

Thermodynamic investigation and environment impact assessment of hydrogen production from steam reforming of poultry tallow  

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Abstract In this research, various assessment tools are applied to comprehensively investigate hydrogen production from steam reforming of poultry tallow (PT). These tools investigate the chemical reactions, design and simulate the entire hydrogen production process, study the energetic performance and perform an environment impact assessment using life cycle assessment (LCA) methodology. The chemical reaction investigation identifies thermodynamically optimal operating conditions at which PT may be converted to hydrogen via the steam reforming process. The synthesis gas composition was determined by simulations to minimize the Gibbs free energy using the Aspen Plus 10.2 software. These optimal conditions are, subsequently, used in the design and simulation of the entire PT-to-hydrogen process. LCA is applied to evaluate the environmental impacts of PT-to-hydrogen system. The system boundaries include rendering and reforming along with the required transportation process. The reforming inventories data are derived from process simulation in Aspen Plus, whereas the rendering data are adapted from a literature review. The life cycle inventories data of PT-to-hydrogen are computationally implemented into SimaPro 7.3. A set of seven relevant environmental impact categories are evaluated: global warming, abiotic depletion, acidification, eutrophication, ozone layer depletion, photochemical oxidant formation, and cumulative non-renewable fossil and nuclear energy demand. The results are subject to a systematic sensitivity analysis and compared to those calculated for hydrogen production from conventional steam methane reforming. The LCA results indicate that the thermal energy production process is the main contributor to the selected environmental impact categories. Improvement actions to minimize the reforming thermal energy and the transport distance are strongly recommended as they would lead to relevant environmental improvements.

Noureddine Hajjaji

2014-01-01T23:59:59.000Z

346

CO-PRODUCTION OF HYDROGEN AND ELECTRICITY USING PRESSURIZED CIRCULATING FLUIDIZED BED GASIFICATION TECHNOLOGY  

SciTech Connect

Foster Wheeler has completed work under a U.S. Department of Energy cooperative agreement to develop a gasification equipment module that can serve as a building block for a variety of advanced, coal-fueled plants. When linked with other equipment blocks also under development, studies have shown that Foster Wheeler's gasification module can enable an electric generating plant to operate with an efficiency exceeding 60 percent (coal higher heating value basis) while producing near zero emissions of traditional stack gas pollutants. The heart of the equipment module is a pressurized circulating fluidized bed (PCFB) that is used to gasify the coal; it can operate with either air or oxygen and produces a coal-derived syngas without the formation of corrosive slag or sticky ash that can reduce plant availabilities. Rather than fuel a gas turbine for combined cycle power generation, the syngas can alternatively be processed to produce clean fuels and or chemicals. As a result, the study described herein was conducted to determine the performance and economics of using the syngas to produce hydrogen for sale to a nearby refinery in a hydrogen-electricity co-production plant setting. The plant is fueled with Pittsburgh No. 8 coal, produces 99.95 percent pure hydrogen at a rate of 260 tons per day and generates 255 MWe of power for sale. Based on an electricity sell price of $45/MWhr, the hydrogen has a 10-year levelized production cost of $6.75 per million Btu; this price is competitive with hydrogen produced by steam methane reforming at a natural gas price of $4/MMBtu. Hence, coal-fueled, PCFB gasifier-based plants appear to be a viable means for either high efficiency power generation or co-production of hydrogen and electricity. This report describes the PCFB gasifier-based plant, presents its performance and economics, and compares it to other coal-based and natural gas based hydrogen production technologies.

Zhen Fan

2006-05-30T23:59:59.000Z

347

Integration of hydrogen management in refinery planning with rigorous process models and product quality specifications  

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New trends of increased heavy crude markets and clean-fuel legislation, to produce ultra low-sulphur (ULS) gasoline and diesel fuels, are forcing refineries to increase their consumption of hydrogen. This critical situation raises the need to have a tool for operating refineries with flexibility and profitability. This paper addresses the planning of refinery with consideration to hydrogen availability. A systematic method for integrating a hydrogen management strategy within a rigorous refinery planning model is undertaken. The presented model consists of two main building blocks: a set of non-linear processing units' models and a hydrogen balance framework. The two blocks are integrated to produce a refinery-wide planning model with hydrogen management. The hydrogen management alternatives were determined by economic analysis. The proposed model improves the hidden hydrogen unavailability that prevents refineries from achieving their maximum production and profit. The model is illustrated on representative case studies and the results are discussed. It was found that an additional annual profit equivalent to $7 million could be achieved with a one-time investment of $13 million in a new purification unit.

Ali Elkamel; Ibrahim Alhajri; A. Almansoori; Yousef Saif

2011-01-01T23:59:59.000Z

348

DOE Workshop on Hydrogen Production via Direct Fermentation  

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Workshop on Workshop on H H Y Y D D R R O O G G E E N N P P R R O O D D U U C C T T I I O O N N V V I I A A D D I I R R E E C C T T F F E E R R M M E E N N T T A A T T I I O O N N June 9, 2004 Baltimore, Maryland DOE-OFFICE OF HYDROGEN, FUEL CELLS AND INFRASTRUCTURE TECHNOLOGIES TABLE OF CONTENTS Introduction................................................................................................................1 Workshop Format ......................................................................................................1 Workshop Results ......................................................................................................2 TABLES Table 1. Results of Group Discussion on Neoterics/NREL Boundary Analysis Report .................................................................................................................

349

High-Performance Bioassisted Nanophotocatalyst for Hydrogen Production  

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Direct conversion of solar energy to chemical fuels such as hydrogen promises technology for providing clean energy in the near future. ... (17) The resultant electrochemical gradient is further converted into chemical energy in the form of ATP that powers the cell. ... Figure 4. (A) IV characteristics of TiO2 and TiO2/bR photoelectrode in dark and light illumination (100 mW/cm2), (B) Energy level diagram showing a possible charge carrier injection in bR/TiO2 in the presence of I/I3 redox species, (C) Short-circuit photocurrent response of TiO2, TiO2/bR, and TiO2/bR bleached electrode in aqueous electrolyte containing 5 mM hydroquinone (HQ) in 10 mM MES, pH 6.2 buffer. ...

Shankar Balasubramanian; Peng Wang; Richard D. Schaller; Tijana Rajh; Elena A. Rozhkova

2013-06-19T23:59:59.000Z

350

An Integrated Hydrogen Production-CO2 Capture Process from Fossil Fuel  

SciTech Connect

The new technology concept integrates two significant complementary hydrogen production and CO{sub 2}-sequestration approaches that have been developed at Oak Ridge National Laboratory (ORNL) and Clark Atlanta University. The process can convert biomass into hydrogen and char. Hydrogen can be efficiently used for stationary power and mobile applications, or it can be synthesized into Ammonia which can be used for CO{sub 2}-sequestration, while char can be used for making time-release fertilizers (NH{sub 4}HCO{sub 3}) by absorption of CO{sub 2} and other acid gases from exhaust flows. Fertilizers are then used for the growth of biomass back to fields. This project includes bench scale experiments and pilot scale tests. The Combustion and Emission Lab at Clark Atlanta University has conducted the bench scale experiments. The facility used for pilot scale tests was built in Athens, GA. The overall yield from this process is 7 wt% hydrogen and 32 wt% charcoal/activated carbon of feedstock (peanut shell). The value of co-product activated carbon is about $1.1/GJ and this coproduct reduced the selling price of hydrogen. And the selling price of hydrogen is estimated to be $6.95/GJ. The green house experimental results show that the samples added carbon-fertilizers have effectively growth increase of three different types of plants and improvement ability of keeping fertilizer in soil to avoid the fertilizer leaching with water.

Zhicheng Wang

2007-03-15T23:59:59.000Z

351

Hydrogen Energy Stations: Poly-Production of Electricity, Hydrogen, and Thermal Energy  

E-Print Network (OSTI)

re-use of thermal energy waste heat for building heating/and thermal energy waste heat, as well as purifiedare used to capture waste heat for productive purposes. Use

Lipman, Timothy; Brooks, Cameron

2006-01-01T23:59:59.000Z

352

DOE Hydrogen Analysis Repository: Water Use for Power Production  

NLE Websites -- All DOE Office Websites (Extended Search)

Water Use for Power Production Water Use for Power Production Project Summary Full Title: Consumptive Water Use for U.S. Power Production Project ID: 205 Principal Investigator: Paul Torcellini Keywords: Water, energy use, electricity generation Purpose Estimate the water consumption at power plants to provide a metric for determining water efficiency in building cooling systems. Performer Principal Investigator: Paul Torcellini Organization: National Renewable Energy Laboratory (NREL) Address: 1617 Cole Blvd. Golden, CO 80401 Telephone: 303-384-7528 Email: paul_torcellini@nrel.gov Additional Performers: R. Judkoff, National Renewable Energy Laboratory; N. Long, National Renewable Energy Laboratory Period of Performance End: December 2003 Project Description Type of Project: Analysis

353

Hydrogen Delivery  

NLE Websites -- All DOE Office Websites (Extended Search)

Mark Paster Energy Efficiency and Renewable Energy Hydrogen, Fuel Cells and Infrastructure Technology Program Hydrogen Production and Delivery Team Hydrogen Delivery Goal Hydrogen Delivery Goal Liquid H 2 & Chem. Carriers Gaseous Pipeline Truck Hydrides Liquid H 2 - Truck - Rail Other Carriers Onsite reforming Develop Develop hydrogen fuel hydrogen fuel delivery delivery technologies that technologies that enable the introduction and enable the introduction and long long - - term viability of term viability of hydrogen as an energy hydrogen as an energy carrier for transportation carrier for transportation and stationary power. and stationary power. Delivery Options * End Game - Pipelines - Other as needed * Breakthrough Hydrogen Carriers * Truck: HP Gas & Liquid Hydrogen

354

Hydrogen production in Multi-Channel Membrane Reactor via Steam Methane Reforming and Methane Catalytic Combustion  

Science Journals Connector (OSTI)

Abstract A novel Multi-Channel Membrane Reactor (MCMR) was designed and built for the small-scale production of hydrogen via Steam Methane Reforming (SMR). The prototype alternates an SMR gas channel to produce hydrogen catalytically, with a Methane Catalytic Combustion (MCC) gas channel to provide the heat of reaction needed by the endothermic reforming. A palladiumsilver membrane inside the reforming gas channel shifts the reaction equilibrium, allowing lower operating temperatures, and producing pure hydrogen in a single vessel. Using an innovative air-spray coating technique, channels were coated with RuMgOLa2O3/?-Al2O3 and Pd/?-Al2O3 catalyst particles for the SMR and MCC reactions, respectively. Results for the proof-of-concept MCMR showed that methane conversion in the reformer of 91% and a hydrogen purity in excess of 99.99% were possible with the reformer operating at 570C and 15bar.

Alexandre Vigneault; John R. Grace

2014-01-01T23:59:59.000Z

355

4 - Hydrogen production in conventional, bio-based and nuclear power plants  

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Abstract: A hydrogen economy advent cannot be based on the current processes and plants, but will need to take advantage of distributed generation systems and to exploit the potential of hydrogen generation in synergy with large electricity or heat generation plants, provided their CO2 emissions are intrinsically low or are abated by means of carbon capture and/or sequestration (CCS) systems. This chapter will focus on real carbon-based energy process appliances and new business cases. A section is also devoted to CCS technologies. Finally, the simultaneous production of hydrogen and power from nuclear plants will be reviewed from a technical point of view, and its future potential impact on the hydrogen economy will be evaluated.

D. Fino

2014-01-01T23:59:59.000Z

356

Investigation of Multistage Circulating Fast Fluidized Bed Membrane Reformers for Production of Ultraclean Hydrogen and Syngas  

Science Journals Connector (OSTI)

Investigation of Multistage Circulating Fast Fluidized Bed Membrane Reformers for Production of Ultraclean Hydrogen and Syngas ... In order to distinguish between the two catalysts employed in this study, the catalyst over which the CSRM and CPOM reactions take place is considered catalyst 1 and that over which the CDRM reaction takes place is considered catalyst 2. The physical significance of catalyst 1 is that both reaction schemes of the CSRM and CPOM are catalyzed by this catalyst to produce hydrogen and syngas and to supply the necessary energy for the heat integration, though catalyst 2 plays an important role to steer the quality of the syngas and to enhance the hydrogen yield. ... In order to check the quality of the corresponding syngas produced in the reaction side, the hydrogen to carbon monoxide feed ratio (H2/CO) profile is presented in Figure 15. ...

Mohamed E. E. Abashar; Said S. E. H. Elnashaie

2014-03-05T23:59:59.000Z

357

Hydrogen Production from Methane Using Oxygen-permeable Ceramic Membranes  

E-Print Network (OSTI)

Non-porous ceramic membranes with mixed ionic and electronic conductivity have received significant interest as membrane reactor systems for the conversion of methane and higher hydrocarbons to higher value products like ...

Faraji, Sedigheh

2010-06-08T23:59:59.000Z

358

Hydrogen production in a reversible flow filtration combustion reactor  

Science Journals Connector (OSTI)

The noncatalytic process of syngas production by means of partial oxidation of ... by air oxygen in a reversible flow filtration combustion reactor has been investigated experimentally. We have ... providing the ...

Yu. M. Dmitrenko; P. A. Klevan

2011-11-01T23:59:59.000Z

359

A Process Model for the Production of Hydrogen Using High Temperature Electrolysis  

SciTech Connect

High temperature electrolysis (HTE) involves the splitting of stream into hydrogen and oxygen at high temperatures. The primary advantage of HTE over conventional low temperature electrolysis is that considerably higher hydrogen production efficiencies can be achieved. Performing the electrolysis process at high temperatures results in more favorable thermodynamics for electrolysis, more efficient production of electricity, and allows direct use of process heat to generate steam. This paper presents the results of process analyses performed to evaluate the hydrogen production efficiencies of an HTE plant coupled to a 600 MWt Modular Helium Reactor (MHR) that supplies both the electricity and process heat needed to drive the process. The MHR operates with a coolant outlet temperature of 950 C. Approximately 87% of the high-temperature heat is used to generate electricity at high efficiency using a direct, Brayton-cycle power conversion system. The remaining high-temperature heat is used to generate a superheated steam / hydrogen mixture that is supplied to the electrolyzers. The analyses were performed using the HYSYS process modeling software. The model used to perform the analyses consisted of three loops; a primary high temperature helium loop, a secondary helium loop and the HTE process loop. The detailed model included realistic representations of all major components in the system, including pumps, compressors, heat exchange equipment, and the electrolysis stack. The design of the hydrogen production process loop also included a steam-sweep gas system to remove oxygen from the electrolysis stack so that it can be recovered and used for other applications. Results of the process analyses showed that hydrogen production efficiencies in the range of 45% to 50% are achievable with this system.

M. G. Mc Kellar; E. A. Harvego; M. Richards; A. Shenoy

2006-07-01T23:59:59.000Z

360

Hydrogen production from methane and solar energy Process evaluations and comparison studies  

Science Journals Connector (OSTI)

Abstract Three conventional and novel hydrogen and liquid fuel production schemes, i.e. steam methane reforming (SMR), solar SMR, and hybrid solar-redox processes are investigated in the current study. H2 (and liquid fuel) productivity, energy conversion efficiency, and associated CO2 emissions are evaluated based on a consistent set of process conditions and assumptions. The conventional SMR is estimated to be 68.7% efficient (HHV) with 90% CO2 capture. Integration of solar energy with methane in solar SMR and hybrid solar-redox processes is estimated to result in up to 85% reduction in life-cycle CO2 emission for hydrogen production as well as 99122% methane to fuel conversion efficiency. Compared to the reforming-based schemes, the hybrid solar-redox process offers flexibility and 6.58% higher equivalent efficiency for liquid fuel and hydrogen co-production. While a number of operational parameters such as solar absorption efficiency, steam to methane ratio, operating pressure, and steam conversion can affect the process performances, solar energy integrated methane conversion processes have the potential to be efficient and environmentally friendly for hydrogen (and liquid fuel) production.

Feng He; Fanxing Li

2014-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


361

The Production of Ethanol and Hydrogen from Pineapple Peel by Saccharomyces Cerevisiae and Enterobacter Aerogenes  

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Abstract The production of biofuels including ethanol and hydrogen from agricultural waste is being concern as a renewable energy. Pineapple peel, a by-product of the pineapple processing industry, account for 29-40% (w/w) of total pineapple weight. 36.252.87% of cellulose was achieved from pineapple peel after pretreatment with water and heat at 100oC for 4h. Afterwards, 0.5% (w/w) cellulase from Aspergillus niger (Sigma) was added for enzymatic hydrolysis. The maximum sugar production (34.031.30g/L) was obtained after 24h of incubation time. The enzyme hydrolysate was utilized as fermentation medium, with no nutritional addition to produce ethanol and hydrogen by Saccharomyces cerevisiae TISTR 5048 and Enterobacter aerogenes TISTR 1468. The maximum yield of ethanol (9.69g/L) with no hydrogen production by S. cerevisiae was achieved after 72h. However, the maximum ethanol and hydrogen from E. aerogenes were 1.38g/L and 1,416mL/L after 72h and 12h of cultivation, respectively. In addition, the 1.2-folds of biofuel production were increased when immobilized bacterial cell in matrix of loofah.

Aophat Choonut; Makorn Saejong; Kanokphorn Sangkharak

2014-01-01T23:59:59.000Z

362

Hydrogen Pathways: Cost, Well-to-Wheels Energy Use, and Emissions for the Current Technology Status of Seven Hydrogen Production, Delivery, and Distribution Scenarios  

NLE Websites -- All DOE Office Websites (Extended Search)

Hydrogen Pathways: Cost, Hydrogen Pathways: Cost, Well-to-Wheels Energy Use, and Emissions for the Current Technology Status of Seven Hydrogen Production, Delivery, and Distribution Scenarios Mark Ruth National Renewable Energy Laboratory Melissa Laffen and Thomas A. Timbario Alliance Technical Services, Inc. Technical Report NREL/TP-6A1-46612 September 2009 Technical Report Hydrogen Pathways: Cost, NREL/TP-6A1-46612 Well-to-Wheels Energy Use, September 2009 and Emissions for the Current Technology Status of Seven Hydrogen Production, Delivery, and Distribution Scenarios Mark Ruth National Renewable Energy Laboratory Melissa Laffen and Thomas A. Timbario Alliance Technical Services, Inc. Prepared under Task No. HS07.1002 National Renewable Energy Laboratory 1617 Cole Boulevard, Golden, Colorado 80401-3393

363

DOE Hydrogen and Fuel Cells Program Record 12001: H2 Production and Delivery Cost Apportionment  

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01 Date: May 14, 2012 01 Date: May 14, 2012 Title: H 2 Production and Delivery Cost Apportionment Originator: Scott Weil, Sara Dillich, Fred Joseck, and Mark Ruth Approved by: Sunita Satyapal and Rick Farmer Date: December 14, 2012 Item: The hydrogen threshold cost is defined as the untaxed cost of hydrogen (H 2 ) (produced, delivered, and dispensed) at which hydrogen fuel cell electric vehicles (FCEVs) are projected to become competitive on a $/mile basis with competing vehicles [gasoline in hybrid-electric vehicles (HEVs)] in 2020. As established in Record 11007 [1], this cost ranges from $2.00-$4.00/gge a of H 2 (based on $2007). The threshold cost can be apportioned into its constituent H 2 production and delivery costs, which can then serve as the respective cost targets for multi-year planning of the Fuel Cell Technologies (FCT)

364

Fuel cells development and hydrogen production from renewable resources in Brazil  

Science Journals Connector (OSTI)

In this work we review the Brazilian energy supply matrix, in particular focusing on environmentally friendly pathways to hydrogen production and fuel cell utilisation. Brazil is currently building capacity in these areas, evident in the spectrum of technological research carried out by several universities in the fields of hydrogen production processes, catalysts and electrolyte materials. Although the fuel cell installed capacity in Brazil is limited, there are several government-funded research activities mainly on PEM, DMFC, DEFC and SOFC, in addition to reforming and catalysis of ethanol as cell fuel. Brazil has a robust energy matrix, and 45% of its energy supply is derived from renewable resources. The future hydrogen economy in Brazil will probably rely on renewable resources, mainly from hydroelectric power and biofuels, which are plentifully available.

D. Hotza; J.C. Diniz da Costa

2008-01-01T23:59:59.000Z

365

Comparative environmental impact and efficiency assessment of selected hydrogen production methods  

Science Journals Connector (OSTI)

Abstract The environmental impacts of various hydrogen production processes are evaluated and compared, considering several energy sources and using life cycle analysis. The results indicate that hydrogen produced by thermochemical water decomposition cycles are more environmentally benign options compared to conventional steam reforming of natural gas. The nuclear based four-step CuCl cycle has the lowest global warming potential (0.559kgCO2-eq per kg hydrogen production), mainly because it requires the lowest quantity of energy of the considered processes. The acidification potential results show that biomass gasification has the highest impact on environment, while wind based electrolysis has the lowest. The relation is also investigated between efficiency and environmental impacts.

Ahmet Ozbilen; Ibrahim Dincer; Marc A. Rosen

2013-01-01T23:59:59.000Z

366

Comparative assessment of hydrogen production methods from renewable and non-renewable sources  

Science Journals Connector (OSTI)

Abstract In this study, we present a comparative environmental impact assessment of possible hydrogen production methods from renewable and non-renewable sources with a special emphasis on their application in Turkey. It is aimed to study and compare the performances of hydrogen production methods and assess their economic, social and environmental impacts, The methods considered in this study are natural gas steam reforming, coal gasification, water electrolysis via wind and solar energies, biomass gasification, thermochemical water splitting with a CuCl and SI cycles, and high temperature electrolysis. Environmental impacts (global warming potential, GWP and acidification potential, AP), production costs, energy and exergy efficiencies of these eight methods are compared. Furthermore, the relationship between plant capacity and hydrogen production capital cost is studied. The social cost of carbon concept is used to present the relations between environmental impacts and economic factors. The results indicate that thermochemical water splitting with the CuCl and SI cycles become more environmentally benign than the other traditional methods in terms of emissions. The options with wind, solar and high temperature electrolysis also provide environmentally attractive results. Electrolysis methods are found to be least attractive when production costs are considered. Therefore, increasing the efficiencies and hence decreasing the costs of hydrogen production from solar and wind electrolysis bring them forefront as potential options. The energy and exergy efficiency comparison study indicates the advantages of biomass gasification over other methods. Overall rankings show that thermochemical CuCl and SI cycles are primarily promising candidates to produce hydrogen in an environmentally benign and cost-effective way.

Canan Acar; Ibrahim Dincer

2014-01-01T23:59:59.000Z

367

The production of pure hydrogen with simultaneous capture of carbon dioxide  

E-Print Network (OSTI)

The need to stabilise or even reduce the production of anthropogenic CO2 makes the capture of CO2 during energy generation from carbonaceous fuels, e.g. coal or biomass, necessary for the future. For hydrogen, an environmentally-benign energy vector...

Bohn, Christopher

2010-10-12T23:59:59.000Z

368

Hydrogen Production by the Thermophilic Alga Mastigocladus laminosus: Effects of Nitrogen, Temperature, and Inhibition of Photosynthesis  

Science Journals Connector (OSTI)

...production of hydrogen by solar radiation was also demonstrated...low-cost culture and H2 collector system, as well as...using specially designed collectors, the heat captured...heat. Thus, the total solar energy conversion efficiency...at a 650 angle to the horizontal and facing southwest...

Kazuhisa Miyamoto; Patrick C. Hallenbeck; John R. Benemann

1979-09-01T23:59:59.000Z

369

Low Cost Hydrogen Production Platform Robert B. Bollinger and Timothy M. Aaron  

E-Print Network (OSTI)

Low Cost Hydrogen Production Platform Robert B. Bollinger and Timothy M. Aaron Praxair, Inc. P.O. Box 44 Tonawanda, NY 14151 Phone: 716-879-2000 Abstract Praxair is in the initial phases of developing. Praxair has as partners in this program, Boothroyd-Dewhurst Inc. (BDI) and Diversified Manufacturing Inc

370

Assessement of Codes and Standards Applicable to a Hydrogen Production Plant Coupled to a Nuclear Reactor  

SciTech Connect

This is an assessment of codes and standards applicable to a hydrogen production plant to be coupled to a nuclear reactor. The result of the assessment is a list of codes and standards that are expected to be applicable to the plant during its design and construction.

M. J. Russell

2006-06-01T23:59:59.000Z

371

Renewable hydrogen production becomes reality at winery Tuesday, September 29, 2009  

E-Print Network (OSTI)

already has on-site wastewater treatment and recycling and the partially treated water from the microbial. -- The first demonstration of a renewable method for hydrogen production from wastewater using a microbial will take winery wastewater, and using bacteria and a small amount of electrical energy, convert the organic

372

ENGINEERING SCALE UP OF RENEWABLE HYDROGEN PRODUCTION BY CATALYTIC STEAM REFORMING OF PEANUT  

E-Print Network (OSTI)

ENGINEERING SCALE UP OF RENEWABLE HYDROGEN PRODUCTION BY CATALYTIC STEAM REFORMING OF PEANUT SHELLS, and academic organizations is developing a steam reforming process to be demonstrated on the gaseous byproducts of this engineering demonstration project. After an initial problem with the heaters that required modification

373

Hydrogen production from inexhaustible supplies of fresh and salt water using microbial  

E-Print Network (OSTI)

Hydrogen production from inexhaustible supplies of fresh and salt water using microbial reverse-electrodialysis, containing exoelectrogenic bacteria, and a cathode, forming a microbial reverse-electrodialysis electrolysis overpotential, while the reverse electrodialysis stack contributed 0.5­0.6 V at a salinity ratio (seawater

374

Materials Development for Improved Efficiency of Hydrogen Production by Steam Electrolysis and Thermochemical-Electrochemical Processes  

E-Print Network (OSTI)

is water electrolysis at high temperatures using heat from a nuclear reactor, known as high temperatureMaterials Development for Improved Efficiency of Hydrogen Production by Steam Electrolysis steam electrolysis (HTSE). The feasibility of this process is currently being demonstrated at Idaho

Yildiz, Bilge

375

Syntrophic interactions drive the hydrogen production from glucose at low temperature in microbial electrolysis cells  

E-Print Network (OSTI)

electrolysis cells Lu Lu a , Defeng Xing a, , Nanqi Ren a , Bruce E. Logan a,b a State Key Laboratory of Urban Water Resource and Environment, School of Municipal and Environmental Engineering, Harbin Institute August 2012 Available online 19 August 2012 Keywords: Hydrogen production Microbial electrolysis cell

376

Hydrogen production from steam reforming of coke oven gas and its utility for indirect reduction of iron oxides in blast  

E-Print Network (OSTI)

of coal and coke are consumed for heating and reducing iron oxides [2,3]. As a result, BFs have becomeHydrogen production from steam reforming of coke oven gas and its utility for indirect reduction 2012 Available online 18 June 2012 Keywords: Steam reforming Hydrogen and syngas production Coke oven

Leu, Tzong-Shyng "Jeremy"

377

Distributed Hydrogen Production from Natural Gas: Independent Review Panel Report  

NLE Websites -- All DOE Office Websites (Extended Search)

Reference herein to any specific commercial product, process, or service by Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States government or any agency thereof. The views and opinions of authors expressed herein do not necessarily state or reflect those of the United States government or any agency thereof. Available electronically at http://www.osti.gov/bridge Available for a processing fee to U.S. Department of Energy and its contractors, in paper, from: U.S. Department of Energy Office of Scientific and Technical Information P.O. Box 62 Oak Ridge, TN 37831-0062 phone: 865.576.8401 fax: 865.576.5728 email: mailto:reports@adonis.osti.gov

378

Hydrogen production by high-temperature steam gasification of biomass and coal  

SciTech Connect

High-temperature steam gasification of paper, yellow pine woodchips, and Pittsburgh bituminous coal was investigated in a batch-type flow reactor at temperatures in the range of 700 to 1,200{sup o}C at two different ratios of steam to feedstock molar ratios. Hydrogen yield of 54.7% for paper, 60.2% for woodchips, and 57.8% for coal was achieved on a dry basis, with a steam flow rate of 6.3 g/min at steam temperature of 1,200{sup o}C. Yield of both the hydrogen and carbon monoxide increased while carbon dioxide and methane decreased with the increase in gasification temperature. A 10-fold reduction in tar residue was obtained at high-temperature steam gasification, compared to low temperatures. Steam and gasification temperature affects the composition of the syngas produced. Higher steam-to-feedstock molar ratio had negligible effect on the amount of hydrogen produced in the syngas in the fixed-batch type of reactor. Gasification temperature can be used to control the amounts of hydrogen or methane produced from the gasification process. This also provides mean to control the ratio of hydrogen to CO in the syngas, which can then be processed to produce liquid hydrocarbon fuel since the liquid fuel production requires an optimum ratio between hydrogen and CO. The syngas produced can be further processed to produce pure hydrogen. Biomass fuels are good source of renewable fuels to produce hydrogen or liquid fuels using controlled steam gasification.

Kriengsak, S.N.; Buczynski, R.; Gmurczyk, J.; Gupta, A.K. [University of Maryland, College Park, MD (United States). Dept. of Mechanical Engineering

2009-04-15T23:59:59.000Z

379

Analysis of Reference Design for Nuclear-Assisted Hydrogen Production at 750C Reactor Outlet Temperature  

SciTech Connect

The use of High Temperature Electrolysis (HTE) for the efficient production of hydrogen without the greenhouse gas emissions associated with conventional fossil-fuel hydrogen production techniques has been under investigation at the Idaho National Engineering Laboratory (INL) for the last several years. The activities at the INL have included the development, testing and analysis of large numbers of solid oxide electrolysis cells, and the analyses of potential plant designs for large scale production of hydrogen using a high-temperature gas-cooled reactor (HTGR) to provide the process heat and electricity to drive the electrolysis process. The results of this research led to the selection in 2009 of HTE as the preferred concept in the U.S. Department of Energy (DOE) hydrogen technology down-selection process. However, the down-selection process, along with continued technical assessments at the INL, has resulted in a number of proposed modifications and refinements to improve the original INL reference HTE design. These modifications include changes in plant configuration, operating conditions and individual component designs. This report describes the resulting new INL reference design coupled to two alternative HTGR power conversion systems, a Steam Rankine Cycle and a Combined Cycle (a Helium Brayton Cycle with a Steam Rankine Bottoming Cycle). Results of system analyses performed to optimize the design and to determine required plant performance and operating conditions when coupled to the two different power cycles are also presented. A 600 MWt high temperature gas reactor coupled with a Rankine steam power cycle at a thermal efficiency of 44.4% can produce 1.85 kg/s of hydrogen and 14.6 kg/s of oxygen. The same capacity reactor coupled with a combined cycle at a thermal efficiency of 42.5% can produce 1.78 kg/s of hydrogen and 14.0 kg/s of oxygen.

Michael G. McKellar; Edwin A. Harvego

2010-05-01T23:59:59.000Z

380

Solar-Powered Electrochemical Oxidation of Organic Compounds Coupled with the Cathodic Production of Molecular Hydrogen  

Science Journals Connector (OSTI)

Solar-Powered Electrochemical Oxidation of Organic Compounds Coupled with the Cathodic Production of Molecular Hydrogen ... The volume percent of the headspace was calculated assuming that it was directly proportional to the ion current measured by the mass spectrometer and that the transfer of all gases through the membrane and their 70 eV electron ionization cross-sections were approximately equivalent. ... In addition, even if hydrogen is mixed with carbon dioxide, CO2 can be readily removed just by chemical absorption process (e.g., flowing carbon dioxide gas through amine solution), which is a typical CO2 separation process in gas turbine power plants. ...

Hyunwoong Park; Chad D. Vecitis; Michael R. Hoffmann

2008-07-26T23:59:59.000Z

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
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they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


381

HYDROGEN PRODUCTION FOR FUEL CELLS VIA REFORMING COAL-DERIVED METHANOL  

SciTech Connect

Hydrogen can be produced from many feedstocks including coal. The objectives of this project are to establish and prove a hydrogen production pathway from coal-derived methanol for fuel cell applications. This progress report is the sixth report submitted to the DOE reporting on the status and progress made during the course of the project. This report covers the time period of January 1-March 31, 2005. This quarter saw progress in four areas. These areas are: (1) Autothermal reforming of coal derived methanol, (2) Catalyst deactivation, (3) Steam reformer transient response, and (4) Catalyst degradation with bluff bodies. All of the projects are proceeding on or slightly ahead of schedule.

Paul A. Erickson

2005-04-01T23:59:59.000Z

382

Assessment Hydrogen Production with CO2 Capture, Volume 1: Baseline State of the Art Plants  

NLE Websites -- All DOE Office Websites (Extended Search)

Hydrogen Hydrogen Production with CO 2 Capture Volume 1: Baseline State-of- the-Art Plants August 30, 2010 DOE/NETL-2010/1434 Disclaimer This report was prepared as an account of work sponsored by an agency of the United States Government. Neither the United States Government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference therein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States

383

Hydrogen Production From Crude Bio-oil and Biomass Char by Electrochemical Catalytic Reforming  

Science Journals Connector (OSTI)

We reports an efficient approach for production of hydrogen from crude bio-oil and biomass char in the dual fixed-bed system by using the electrochemical catalytic reforming method. The maximal absolute hydrogen yield reached 110.9 g H2/kg dry biomass. The product gas was a mixed gas containing 72%H2, 26%CO2, 1.9%CO, and a trace amount of CH4. It was observed that adding biomass char (a by-product of pyrolysis of biomass) could remarkably increase the absolute H2 yield (about 20%-50%). The higher reforming temperature could enhance the steam reforming reaction of organic compounds in crude bio-oil and the reaction of CO and H2O. In addition, the CuZn-Al2O3 catalyst in the water-gas shift bed could also increase the absolute H2 yield via shifting CO to CO2.

Xing-long Li; Shen Ning; Li-xia Yuan; Quan-xin Li

2011-01-01T23:59:59.000Z

384

Hydrogen production in ultrarich combustion of hydrocarbon fuels in porous media  

Science Journals Connector (OSTI)

Rich and ultrarich combustion of methane, ethane, and propane inside inert porous media is studied experimentally and numerically to examine the suitability of the concept for hydrogen production. Temperature, velocities, and chemical products of the combustion waves were recorded experimentally at a range of equivalence ratios from stoichiometry (?=1.0) to ?=2.5, for a filtration velocity of 12cm/s. Two-temperature numerical model based on comprehensive heat transfer and chemical mechanisms is found to be in a good qualitative agreement with experimental data. Partial oxidation products of methane, ethane, and propane (H2, CO, and C2 hydrocarbons) are dominant for ultrarich superadiabatic combustion. The maximum hydrogen yield is close to 50% for all fuels, and carbon monoxide yield is close to 80%.

Mario Toledo; Valeri Bubnovich; Alexei Saveliev; Lawrence Kennedy

2009-01-01T23:59:59.000Z

385

Comparison of several glycerol reforming methods for hydrogen and syngas production using Gibbs energy minimization  

Science Journals Connector (OSTI)

Abstract This paper focuses on the comparison of different glycerol reforming technologies aimed to hydrogen and syngas production. The reactions of steam reforming, partial oxidation, autothermal reforming, dry reforming and supercritical water gasification were analyzed. For this, the Gibbs energy minimization approach was used in combination with the virial equation of state. The validation of the model was made between the simulations of the proposed model and both, simulated and experimental data obtained in the literature. The effects of modifications in the operational temperature, operational pressure and reactants composition were analyzed with regard to composition of the products. The effect of coke formation was discussed too. Generally, higher temperatures and lower pressures resulted in higher hydrogen and syngas production. All reforming technologies demonstrated to be feasible for use in hydrogen or synthesis gas production in respect of the products composition. The proposed model showed good predictive ability and low computational time (close to 1s) to perform the calculation of the combined chemical and phase equilibrium for all systems analyzed.

Antonio C.D. Freitas; Reginaldo Guirardello

2014-01-01T23:59:59.000Z

386

Low-Cost Hydrogen-from-Ethanol: A Distributed Production System (Presentation)  

NLE Websites -- All DOE Office Websites (Extended Search)

Hydrogen-from- Hydrogen-from- Ethanol: A Distributed Production System Presented at the Bio-Derived Liquids to Hydrogen Distributed Reforming Working Group Meeting Laurel, Maryland Tuesday, November 6, 2007 H 2 Gen Innovations, Inc. Alexandria, Virginia www.h2gen.com 2 Topics * H 2 Gen Reformer System Innovation * Natural Gas Reformer - Key performance metrics - Summary unique H2A inputs * Ethanol Reformer - Key performance metrics - Summary unique H2A inputs * Questions from 2007 Merit Review 3 H 2 Gen Innovations' Commercial SMR * Compact, low-cost 115 kg/day natural gas reformer proven in commercial practice [13 US Patents granted] * Built-in, unique, low-cost PSA system * Unique sulfur-tolerant catalyst developed with Süd Chemie 4 DOE Program Results * Task 1- Natural Gas Reformer Scaling:

387

Hydrogen Production by Catalytic Steam Reforming of Bio-oil, Naphtha  

Science Journals Connector (OSTI)

Hydrogen production by catalytic steam reforming of the bio-oil, naphtha, and CH4 was investigated over a novel metal-doped catalyst of (Ca24Al28O64)4+4O?/Mg (C12A7-Mg). The catalytic steam reforming was investigated from 250 to 850C in the fixed-bed continuous flow reactor. For the reforming of bio-oil, the yield of hydrogen of 80% was obtained at 750C, and the maximum carbon conversion is nearly close to 95% under the optimum steam reforming condition. For the reforming of naphtha and CH4, the hydrogen yield and carbon conversion are lower than that of bio-oil at the same temperature. The characteristics of catalyst were also investigated by XPS. The catalyst deactivation was mainly caused by the deposition of carbon in the catalytic steam reforming process.

Yue Pan; Zhao-xiang Wang; Tao Kan; Xi-feng Zhu; Quan-xin Li

2006-01-01T23:59:59.000Z

388

The Hype About Hydrogen  

E-Print Network (OSTI)

economy based on the hydrogen fuel cell, but this cannot beus to look toward hydrogen. Fuel cell basics, simplifiedthe path to fuel cell commercialization. Hydrogen production

Mirza, Umar Karim

2006-01-01T23:59:59.000Z

389

Thermodynamic Analysis of the Possibility of Hydrogen Production by Oxidation of n-Butane, n-Pentane, and Carbon by Oxygen-Containing Nitrogen Compounds  

Science Journals Connector (OSTI)

A thermodynamic analysis is performed to study the reactions of hydrogen production by oxidation of hydrocarbons of natural gas ... analysis suggests the possibility of developing a new hydrogen production method

A. M. Alekseev; Z. V. Komova; L. L. Klinova

2003-07-01T23:59:59.000Z

390

Assessment of Hydrogen Production Systems based on Natural Gas Conversion with Carbon Capture and Storage  

Science Journals Connector (OSTI)

Abstract Introduction of hydrogen in the energy system, as a new energy carrier complementary to electricity, is exciting much interest not only for heat and power generation applications, but also for transport and petro-chemical sectors. In transition to a low carbon economy, Carbon Capture and Storage (CCS) technologies represent another way to reduce CO2 emissions. Hydrogen can be produced from various feedstocks, the most important being based on fossil fuels (natural gas and coal). This paper investigates the techno-economic and environmental aspects of hydrogen production based on natural gas reforming conversion with and without carbon capture. As CO2 capture options, gas - liquid absorption and chemical looping were evaluated. The evaluated plant concepts generate 300MWth hydrogen (based on hydrogen LHV) with purity higher than 99.95 % (vol.), suitable to be used both in petro-chemical applications as well as for Proton Exchange Membrane (PEM) fuel cells for mobile applications. For the designs with CCS, the carbon capture rate is about 70 % for absorption-based scheme while for chemical looping-based system is >99 %. Special emphasis is put in the paper on the assessment of various plant configurations and process integration issues using CAPE techniques. The mass and energy balances have been used furthermore for techno-economic and environmental impact assessments.

Calin-Cristian Cormos; Letitia Petrescu; Ana-Maria Cormos

2014-01-01T23:59:59.000Z

391

Hydrogen Pathways: Updated Cost, Well-to-Wheels Energy Use, and Emissions for the Current Technology Status of Ten Hydrogen Production, Delivery, and Distribution Scenarios  

SciTech Connect

This report describes a life-cycle assessment conducted by the National Renewable Energy Laboratory (NREL) of 10 hydrogen production, delivery, dispensing, and use pathways that were evaluated for cost, energy use, and greenhouse gas (GHG) emissions. This evaluation updates and expands on a previous assessment of seven pathways conducted in 2009. This study summarizes key results, parameters, and sensitivities to those parameters for the 10 hydrogen pathways, reporting on the levelized cost of hydrogen in 2007 U.S. dollars as well as life-cycle well-to-wheels energy use and GHG emissions associated with the pathways.

Ramsden, T.; Ruth, M.; Diakov, V.; Laffen, M.; Timbario, T. A.

2013-03-01T23:59:59.000Z

392

Bio-hydrogen production from cornstalk wastes by orthogonal design method  

Science Journals Connector (OSTI)

One-factor-at-a-time design and orthogonal design were used in the experimental design methods to optimize bio-hydrogen (bio-H2) production from cornstalk wastes by anaerobic fermentation. Three series of experiments were designed to investigate the effects of substrate concentration, initial pH and orthogonal design on the bio-H2 production by using the natural sludge as inoculant. Experimental results indicate that substrate concentration was the most significant condition for optimal hydrogen production. The optimum orthogonal design method was proposed to be at an enzymatic temperature of 50C, an enzymatic time of 72h, an initial pH of 7.0 and a substrate concentration of 10g/L. The proposed method facilitated the optimization of optimum design parameters, only with a few well-defined experimental sets. Under the proposed condition, the maximum cumulative H2 yield was 141.29mlg?1-CS (cornstalk, or 164.48mlg?1-TS, total solid, TS=0.859 Wdried cornstalk), with an average H2 production rate of 12.31mlg?1-CSh?1. The hydrogen content reached 57.85% and methane was not detected in the biogas.

Shenghua Ma; Hui Wang; Yu Wang; Huaiyu Bu; Jinbo Bai

2011-01-01T23:59:59.000Z

393

ENHANCED HYDROGEN PRODUCTION INTEGRATED WITH CO2 SEPARATION IN A SINGLE-STAGE REACTOR  

SciTech Connect

The water gas shift reaction (WGSR) plays a major role in increasing the hydrogen production from fossil fuels. However, the enhanced hydrogen production is limited by thermodynamic constrains posed by equilibrium limitations of WGSR. This project aims at using a mesoporous, tailored, highly reactive calcium based sorbent system for incessantly removing the CO{sub 2} product which drives the equilibrium limited WGSR forward. In addition, a pure sequestration ready CO{sub 2} stream is produced simultaneously. A detailed project vision with the description of integration of this concept with an existing coal gasification process for hydrogen production is presented. Conceptual reactor designs for investigating the simultaneous water gas shift and the CaO carbonation reactions are presented. In addition, the options for conducting in-situ sorbent regeneration under vacuum or steam are also reported. Preliminary, water gas shift reactions using high temperature shift catalyst and without any sorbent confirmed the equilibrium limitation beyond 600 C demonstrating a carbon monoxide conversion of about 80%. From detailed thermodynamic analyses performed for fuel gas streams from typical gasifiers the optimal operating temperature range to prevent CaO hydration and to effect its carbonation is between 575-830 C.

Himanshu Gupta; Mahesh Iyer; Bartev Sakadjian; Liang-Shih Fan

2005-03-10T23:59:59.000Z

394

Thermodynamics of Hydrogen Production from Dimethyl Ether Steam Reforming and Hydrolysis  

SciTech Connect

The thermodynamic analyses of producing a hydrogen-rich fuel-cell feed from the process of dimethyl ether (DME) steam reforming were investigated as a function of steam-to-carbon ratio (0-4), temperature (100 C-600 C), pressure (1-5 atm), and product species: acetylene, ethanol, methanol, ethylene, methyl-ethyl ether, formaldehyde, formic acid, acetone, n-propanol, ethane and isopropyl alcohol. Results of the thermodynamic processing of dimethyl ether with steam indicate the complete conversion of dimethyl ether to hydrogen, carbon monoxide and carbon dioxide for temperatures greater than 200 C and steam-to-carbon ratios greater than 1.25 at atmospheric pressure (P = 1 atm). Increasing the operating pressure was observed to shift the equilibrium toward the reactants; increasing the pressure from 1 atm to 5 atm decreased the conversion of dimethyl ether from 99.5% to 76.2%. The order of thermodynamically stable products in decreasing mole fraction was methane, ethane, isopropyl alcohol, acetone, n-propanol, ethylene, ethanol, methyl-ethyl ether and methanol--formaldehyde, formic acid, and acetylene were not observed. The optimal processing conditions for dimethyl ether steam reforming occurred at a steam-to-carbon ratio of 1.5, a pressure of 1 atm, and a temperature of 200 C. Modeling the thermodynamics of dimethyl ether hydrolysis (with methanol as the only product considered), the equilibrium conversion of dimethyl ether is limited. The equilibrium conversion was observed to increase with temperature and steam-to-carbon ratio, resulting in a maximum dimethyl ether conversion of approximately 68% at a steam-to-carbon ratio of 4.5 and a processing temperature of 600 C. Thermodynamically, dimethyl ether processed with steam can produce hydrogen-rich fuel-cell feeds--with hydrogen concentrations exceeding 70%. This substantiates dimethyl ether as a viable source of hydrogen for PEM fuel cells.

T.A. Semelsberger

2004-10-01T23:59:59.000Z

395

Polygeneration-IGCC concepts for the production of hydrogen rich fuels based on lignite  

Science Journals Connector (OSTI)

This paper presents three IGCC-power plant concepts for central production of a hydrogen-rich fuel (methanol, hydrogen, synthetic natural gas ?? SNG) from lignite. Each concept contains a CO2-separation, which produces a sequestration-ready CO2-rich stream. Thus, CO2-emissions caused by use of lignite are considerably reduced. Furthermore, the produced low-carbon fuels are converted in decentralised Combined Heat and Power Plants (CHPP). CHPP leads to high efficiencies of fuel utilisation between 54 and 62%, which exceed the efficiencies of single power generation. Regarding to the CO2-emissions of a natural gas fired CHPP, heat and power can be generated by lignite as clean as by natural gas. The specific CO2-emissions are even much lower in the case of hydrogen production. Costs for the centrally produced methanol and hydrogen are with 29 and 19 EUR/MWh(LHV) already within an economic range. Synthetic natural gas can be produced for 23 EUR/MWh(LHV).

Bernd Meyer; Katrin Ogriseck

2007-01-01T23:59:59.000Z

396

Assessment of a new integrated solar energy system for hydrogen production  

Science Journals Connector (OSTI)

Abstract In this paper, a novel integrated system that combines photocatalysis, photovoltaics, thermal engine and chemical energy storage for better solar energy harvesting is assessed using energy and exergy methods. The system generates hydrogen and sulfur from sulfurous waters specific to chemical and petrochemical industries. The solar light is split into three spectra using optical surfaces covered with selected dielectric coatings: (i) the high energy spectrum, consisting of photons with wavelengths shorter than ?500nm, is used to generate hydrogen from water photolysis, (ii) the middle spectrum with wavelengths between ?500nm and ?800nm is used to generate electricity with photovoltaic (PV) arrays and (iii) the long wave spectrum of low energy photons with wavelengths longer than ?800nm is used to generate electricity with a thermally driven Rankine engine (RE). The electricity generated by PV and RE is employed to generate additional hydrogen by electrolysis and to drive auxiliary devices within the system. A model is developed based on conservation equations and transport equations applied for each essential component of the system. The model allows for assessment of system performance and the comparison with other solar hydrogen production systems. A case study for an oil sands exploitation area where sulfurous aqueous wastes and hydrogen demand exist Calgary (Alberta) is presented. A solar tower configuration is selected as the best choice for a large scale system with 500MW light harvesting heliostat field. Hourly predictions of system output are obtained. The devised system requires 5526acres of land for the solar field and produces 41.4t hydrogen per day. If a conventional solar tower would be used instead which generates power and is coupled to a water electrolysis system the hydrogen production is lower, namely 28.7t/day. An economic scenario is considered by assuming that the co-produced sulfur and hydrogen are both valorized on the market for 25years with a levelized price of 1.65$/kg out of which 10% represents operation and maintenance costs. It is shown that the system is feasible provided that the required equity investment of capital is inferior to M$ 500.

C. Zamfirescu; I. Dincer

2014-01-01T23:59:59.000Z

397

Renewable Hydrogen: Technology Review and Policy Recommendations for State-Level Sustainable Energy Futures  

E-Print Network (OSTI)

Review of Hydrogen Production Methods Renewable HydrogenResearch on Hydrogen Production Methods Hydrogen ProductionRenewable Hydrogen Production Methods The most common

Lipman, Timothy; Edwards, Jennifer Lynn; Brooks, Cameron

2006-01-01T23:59:59.000Z

398

FutureGen Technologies for Carbon Capture and Storage and Hydrogen and Electricity Production  

NLE Websites -- All DOE Office Websites (Extended Search)

FutureGen FutureGen Technologies for Carbon Capture and Storage and Hydrogen and Electricity Production Office of Fossil Energy U. S. Department of Energy Washington, DC June 2, 2003 Lowell Miller, Director, Office of Coal & Power Systems 24-Jun-03 Slide 2 Office of Fossil Energy Presentation Agenda * FE Hydrogen Program * FutureGen * Carbon Sequestration Leadership Forum (CSLF) 24-Jun-03 Slide 3 Office of Fossil Energy Key Drivers * Decreasing domestic supply will lead to increased imports from less stable regions * Conventional petroleum is finite; production will peak and irreversibly decline due to continually increasing demand * Improving environmental quality - Meeting air emission regulations - Greenhouse gas emissions 0 2 4 6 8 10 12 14 16 18 20 1970 1975 1980 1985 1990 1995 2000 2005

399

Metabolic engineering of Caldicellulosiruptor bescii yields increased hydrogen production from lignocellulosic biomass  

NLE Websites -- All DOE Office Websites (Extended Search)

Metabolic Metabolic engineering of Caldicellulosiruptor bescii yields increased hydrogen production from lignocellulosic biomass Minseok Cha 1,3 , Daehwan Chung 1,3 , James G Elkins 2,3 , Adam M Guss 2,3 and Janet Westpheling 1,3* Abstract Background: Members of the anaerobic thermophilic bacterial genus Caldicellulosiruptor are emerging candidates for consolidated bioprocessing (CBP) because they are capable of efficiently growing on biomass without conventional pretreatment. C. bescii produces primarily lactate, acetate and hydrogen as fermentation products, and while some Caldicellulosiruptor strains produce small amounts of ethanol C. bescii does not, making it an attractive background to examine the effects of metabolic engineering. The recent development of methods for genetic manipulation has set the stage for rational engineering of this genus for improved biofuel

400

Dynamical safety assessment of hydrogen production nuclear power plants using system dynamics method  

Science Journals Connector (OSTI)

Nuclear power plants for hydrogen production are investigated in the aspect of nuclear safety. The non-linear dynamical safety assessment is introduced for the analysis of the high temperature gas cooled reactor (HTGR) which is used for hydrogen production as well as electricity generation. The dynamical algorithm is adjusted for the safety assessment with an easier and reliable output. A feedback of power increase affects to the temperature decrease. The top event of the event is power and temperature stable. It is affected by the human factor, poison, and some other physical variables. There are several factors including the economic and safety factors which are considered for the reliability of the modelling simulations. Using the system dynamics (SD) method, the event quantification is performed for the event flows, stocks, and feedback by the single and double arrow lines.

Taeho Woo; Soonho Lee

2013-01-01T23:59:59.000Z

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


401

Carbonaceous material for production of hydrogen from low heating value fuel gases  

DOE Patents (OSTI)

A process for the catalytic production of hydrogen, from a wide variety of low heating value fuel gases containing carbon monoxide, comprises circulating a carbonaceous material between two reactors--a carbon deposition reactor and a steaming reactor. In the carbon deposition reactor, carbon monoxide is removed from a fuel gas and is deposited on the carbonaceous material as an active carbon. In the steaming reactor, the reactive carbon reacts with steam to give hydrogen and carbon dioxide. The carbonaceous material contains a metal component comprising from about 75% to about 95% cobalt, from about 5% to about 15% iron, and up to about 10% chromium, and is effective in suppressing the production of methane in the steaming reactor.

Koutsoukos, Elias P. (Los Angeles, CA)

1989-01-01T23:59:59.000Z

402

Enhanced Hydrogen Production in Escherichia coli Through Chemical Mutagenesis, Gene Deletion, and Transposon Mutagenesis  

E-Print Network (OSTI)

A ............................................................................... 12 Figure 3-2. Modified complex formate agar screening plates with 100 ?g/ml Kan and 0.5 mM IPTG for identifying colonies with enhanced hydrogen production... electrodes (6, 60); therefore, in the future, biohydrogen could play an important role as a new energy source and replace batteries and fuels that when are burned releases hazardous compounds to the environmental media. E. coli is a facultative anaerobe...

Garzon Sanabria, Andrea Juliana

2011-08-08T23:59:59.000Z

403

Nitrogen-Doped Anatase Nanofibers Decorated with Noble Metal Nanoparticles for Photocatalytic Production of Hydrogen  

Science Journals Connector (OSTI)

Nitrogen-Doped Anatase Nanofibers Decorated with Noble Metal Nanoparticles for Photocatalytic Production of Hydrogen ... High-aspect-ratio titanate nanotubes (NT) and nanowires (NW) were produced by the hydrothermal conversion of TiO2 at 400 K. ... Two novel deposition methods were used to synthesize Pt-TiO2 composite photoelectrodes: a tilt-target room temperature sputtering method and aerosol-chemical vapor deposition (ACVD). ...

Ming-Chung Wu; Jussi Hiltunen; Andrs Spi; Anna Avila; William Larsson; Hsueh-Chung Liao; Mika Huuhtanen; Gza Tth; Andrey Shchukarev; Nomi Laufer; kos Kukovecz; Zoltn Knya; Jyri-Pekka Mikkola; Riitta Keiski; Wei-Fang Su; Yang-Fang Chen; Heli Jantunen; Pulickel M. Ajayan; Robert Vajtai; Krisztin Kords

2011-05-13T23:59:59.000Z

404

Lattice Defect-Enhanced Hydrogen Production in Nanostructured Hematite-Based Photoelectrochemical Device  

Science Journals Connector (OSTI)

Lattice Defect-Enhanced Hydrogen Production in Nanostructured Hematite-Based Photoelectrochemical Device ... methods for the codeposition of Cr or Mo with ?-Fe2O3 (hematite) were developed to produce doped Fe oxide films with varying compns. of Cr and Mo which are active photoanodes for photoelectrochem. ... Photoelectrochemical (PEC) water splitting to produce H2 is a renewable method for addressing the worldwide energy consumption increasing and fossil fuels storage shrinking. ...

Peng Wang; Degao Wang; Jun Lin; Xiaolong Li; Cheng Peng; Xingyu Gao; Qing Huang; Jianqiang Wang; Hongjie Xu; Chunhai Fan

2012-03-27T23:59:59.000Z

405

Evaluation of the Potential Environmental Impacts from Large-Scale Use and Production of Hydrogen in Energy and Transportation Applications  

SciTech Connect

The purpose of this project is to systematically identify and examine possible near and long-term ecological and environmental effects from the production of hydrogen from various energy sources based on the DOE hydrogen production strategy and the use of that hydrogen in transportation applications. This project uses state-of-the-art numerical modeling tools of the environment and energy system emissions in combination with relevant new and prior measurements and other analyses to assess the understanding of the potential ecological and environmental impacts from hydrogen market penetration. H2 technology options and market penetration scenarios will be evaluated using energy-technology-economics models as well as atmospheric trace gas projections based on the IPCC SRES scenarios including the decline in halocarbons due to the Montreal Protocol. Specifically we investigate the impact of hydrogen releases on the oxidative capacity of the atmosphere, the long-term stability of the ozone layer due to changes in hydrogen emissions, the impact of hydrogen emissions and resulting concentrations on climate, the impact on microbial ecosystems involved in hydrogen uptake, and criteria pollutants emitted from distributed and centralized hydrogen production pathways and their impacts on human health, air quality, ecosystems, and structures under different penetration scenarios

Wuebbles, D.J.; Dubey, M.K., Edmonds, J.; Layzell, D.; Olsen, S.; Rahn, T.; Rocket, A.; Wang, D.; Jia, W.

2010-06-01T23:59:59.000Z

406

Fuel Cell Technologies Office Multi-Year Research, Development, and Demonstration Plan- Section 3.1 Hydrogen Production  

Energy.gov (U.S. Department of Energy (DOE))

Hydrogen Production technical plan section of the Fuel Cell Technologies Office Multi-Year Research, Development, and Demonstration Plan; updated October 2014. This plan includes goals, objectives, technical targets, tasks, and schedules for the Office of Energy Efficiency and Renewable Energy's contribution to the DOE Hydrogen and Fuel Cells Program.

407

Systematics of isotopic production cross sections from interactions of relativistic 40Ca in hydrogen  

Science Journals Connector (OSTI)

The isotopic production cross sections for 40Ca projectiles at 357, 565, and 763 MeV/nucleon interacting in a liquid hydrogen target have been measured by the Transport Collaboration at the LBL HISS facility. The systematics of these cross sections are studied, and the results indicate that nuclear structure effects are present in the isotope production process during the relativistic collisions. The newly measured cross sections are also compared with those predicted by semiempirical and parametric formulas, but the predictions do not fully describe the systematics such as the energy dependence. The consequences of the cross section systematics in galactic cosmic ray studies are also discussed.

C.-X. Chen; S. Albergo; Z. Caccia; S. Costa; H. J. Crawford; M. Cronqvist; J. Engelage; L. Greiner; T. G. Guzik; A. Insolia; C. N. Knott; P. J. Lindstrom; M. McMahon; J. W. Mitchell; R. Potenza; G. V. Russo; A. Soutoul; O. Testard; C. E. Tull; C. Tuv; C. J. Waddington; W. R. Webber; J. P. Wefel

1997-09-01T23:59:59.000Z

408

Removal of hydrogen sulfide as ammonium sulfate from hydropyrolysis product vapors  

SciTech Connect

A system and method for processing biomass into hydrocarbon fuels that includes processing a biomass in a hydropyrolysis reactor resulting in hydrocarbon fuels and a process vapor stream and cooling the process vapor stream to a condensation temperature resulting in an aqueous stream. The aqueous stream is sent to a catalytic reactor where it is oxidized to obtain a product stream containing ammonia and ammonium sulfate. A resulting cooled product vapor stream includes non-condensable process vapors comprising H.sub.2, CH.sub.4, CO, CO.sub.2, ammonia and hydrogen sulfide.

Marker, Terry L; Felix, Larry G; Linck, Martin B; Roberts, Michael J

2014-10-14T23:59:59.000Z

409

Electron Source in Photoinduced Hydrogen Production on Pt-supported TiO2 Particles  

Science Journals Connector (OSTI)

Electron Source in Photoinduced Hydrogen Production on Pt-supported TiO2 Particles ... After recovering the TiO2/Pt particles used in the long-term reaction, they were reused in a photocatalytic H+ reduction by adding methanol as an electron donor, but no H2 production was observed showing that the TiO2/Pt particles have lost their photocatalytic activity after the long-term reaction. ... A 100 W high-pressure Hg lamp was used as a light source. ...

Toshiyuki Abe; Eiji Suzuki; Kentaro Nagoshi; Kohichi Miyashita; Masao Kaneko

1999-02-04T23:59:59.000Z

410

The Transition to Hydrogen  

E-Print Network (OSTI)

above, not all hydrogen production methods are equal inrealize hydrogens bene- ?ts fully, production methods thathydrogen vary depending on which primary source produces it and which production method

Ogden, Joan M

2005-01-01T23:59:59.000Z

411

Production and use of electrolytic hydrogen in Ecuador towards a low carbon economy  

Science Journals Connector (OSTI)

Abstract This paper presents a pre-feasibility study of producing and using electrolytic hydrogen in Ecuador as part of a strategy towards a low carbon economy. Hydrogen could be produced using hydropower either alone or combined with other renewable energy sources. For this study, we analyzed two scenarios of energy availability based on data from the largest hydroelectric power plant in the country. The first scenario assumes that an amount of water equivalent to 30% of that spilled in 2011 could be used to generate additional electricity. Thus, an additional amount of energy equivalent to 5% of the energy produced in 2011 could be available. The second scenario doubles this amount of energy. Economic analysis showed that to obtain low-cost hydrogen (3.00US$/kg) it is necessary to operate the electrolysis plants 24h/day, using low-cost electricity (30US$/MWh). A continuous supply of energy could be possible when new hydroelectric utilities start operating or by integrating hydropower with solar and wind. Three possibilities for using hydrogen are discussed: 1) production of ammonia as a raw material for nitrogenous fertilizers, 2) hydro-treating heavy oils and bio-oils in oil refineries, and 3) as an energy storage medium to offset natural instability and unpredictability of renewables.

Manuel Raul Pelaez-Samaniego; Gustavo Riveros-Godoy; Santiago Torres-Contreras; Tsai Garcia-Perez; Esteban Albornoz-Vintimilla

2014-01-01T23:59:59.000Z

412

Economic Analysis of the Reference Design for a Nuclear-Driven High-Temperature-Electrolysis Hydrogen Production Plant  

SciTech Connect

A reference design for a commercial-scale high-temperature electrolysis (HTE) plant for hydrogen production was developed to provide a basis for comparing the HTE concept with other hydrogen production concepts. The reference plant design is driven by a high-temperature helium-cooled reactor coupled to a direct Brayton power cycle. The reference design reactor power is 600 MWt, with a primary system pressure of 7.0 MPa, and reactor inlet and outlet fluid temperatures of 540C and 900C, respectively. The electrolysis unit used to produce hydrogen consists of 4,009,177 cells with a per-cell active area of 225 cm2. A nominal cell area-specific resistance, ASR, value of 0.4 Ohmcm2 with a current density of 0.25 A/cm2 was used, and isothermal boundary conditions were assumed. The optimized design for the reference hydrogen production plant operates at a system pressure of 5.0 MPa, and utilizes an air-sweep system to remove the excess oxygen that is evolved on the anode side of the electrolyzer. The inlet air for the air-sweep system is compressed to the system operating pressure of 5.0 MPa in a four-stage compressor with intercooling. The alternating current, AC, to direct current, DC, conversion is 96%. The overall system thermal-to-hydrogen production efficiency (based on the low heating value of the produced hydrogen) is 47.12% at a hydrogen production rate of 2.356 kg/s. An economic analysis of the plant was also performed using the H2A Analysis Methodology developed by the Department of Energy (DOE) Hydrogen Program. The results of the economic analysis demonstrated that the HTE hydrogen production plant driven by a high-temperature helium-cooled nuclear power plant can deliver hydrogen at a competitive cost using realistic financial and cost estimating assumptions. A required cost of $3.23 per kg of hydrogen produced was calculated assuming an internal rate of return of 10%. Approximately 73% of this cost ($2.36/kg) is the result of capital costs associated with the construction of the combined nuclear plant and hydrogen production facility. Operation and maintenance costs represent about 18% of the total cost ($0.57/kg). Variable costs (including the cost of nuclear fuel) contribute about 8.7% ($0.28/kg) to the total cost of hydrogen production, and decommissioning and raw material costs make up the remaining fractional cost.

E. A. Harvego; M. G. McKellar; M. S. Sohal; J. E. O'Brien; J. S. Herring

2008-01-01T23:59:59.000Z

413

2009 Pathways to Commercial Success: Technologies and Products Supported by the Hydrogen, Fuel Cells and Infrastructure Technologies Program  

Energy.gov (U.S. Department of Energy (DOE))

This report documents the results of an effort to identify and characterize commercial and emerging technologies and products that benefited from the support of the Hydrogen, Fuel Cells and Infrastructure Technologies Program.

414

Experimental forward and reverse in situ combustion gasification of lignite with production of hydrogen-rich syngas  

Science Journals Connector (OSTI)

This research focused on the feasibility of applying the forward and reverse combustion approach to the in situ gasification of lignite with the production of hydrogen-rich syngas (H2 and CO). The so-called forwa...

Yong Cui; Jie Liang; Zhangqing Wang

2014-03-01T23:59:59.000Z

415

Pathways to Commercial Success: Technologies and Products Supported by the Hydrogen, Fuel Cells and Infrastructure Technologies Program  

Fuel Cell Technologies Publication and Product Library (EERE)

This report documents the results of an effort to identify and characterize commercial and near-commercial (emerging) technologies and products that benefited from the support of the Hydrogen, Fuel Ce

416

The Hydrogen Policy Survey: Descriptive Statistics of the Study Sample and Their Policy Perspectives  

E-Print Network (OSTI)

Hydrogen production Hydrogen storage technology Hydrogensub-freezing operation Hydrogen storage Hydrogen delivery COand development of hydrogen storage and hydrogen production

Collantes, Gustavo O

2005-01-01T23:59:59.000Z

417

THE HYDROGEN POLICY SURVEY: DESCRIPTIVE STATISTICS OF THE STUDY SAMPLE AND THEIR POLICY PERSPECTIVES  

E-Print Network (OSTI)

Hydrogen production Hydrogen storage technology Hydrogensub-freezing operation Hydrogen storage Hydrogen delivery COand development of hydrogen storage and hydrogen production

Collantes, G O

2005-01-01T23:59:59.000Z

418

Thermophilic hydrogen production from starch wastewater using two-phase sequencing batch fermentation coupled with UASB methanogenic effluent recycling  

Science Journals Connector (OSTI)

Abstract The aim of this study was to evaluate the performance of thermophilic hydrogenesis coupled with mesophilic methanogenesis in which the effluent was recycled to the hydrogen reactor for starch wastewater treatment. With this system, the hydrogen production rate and yield were 3.450.25L H2/(Ld) and 5.790.41mmol H2/g \\{CODadded\\} respectively, and thus higher than the values of the control group without methanogenic effluent recycling. In addition, relatively higher contents of acetate and butyrate were obtained in the hydrogen reactor with recirculation. The methane reactors were operated with the effluent from the hydrogen reactor, and methane yield was stabilized at 0.210.23L/g \\{CODremoval\\} in both. Analysis of the microbial communities further showed that methanogenic effluent recirculation enriched microbial communities in the hydrogen reactor. Two species of bacteria effective in hydrogenesis, Thermoanaerobacterium thermosaccharolyticum and Clostridium thermosaccharolyticum, dominated during hydrogen production, whereas archaea belonging to Euryarchaeota were detected and cultured in the methane reactor. The recycled effluent supplied alkaline substrates for the hydrogen producing bacteria. Alkali balance calculations showed that the amount of added alkali was reduced by 88%. This amount, required for hydrogen production from starch wastewater, was contributed by alkali in the methanogenic effluent, (2225140mg CaCO3/L), resulting in lower operational costs.

Li Xie; Nanshi Dong; Lei Wang; Qi Zhou

2014-01-01T23:59:59.000Z

419

Hydrogen Production Performance of a 10-Cell Planar Solid-Oxide Electrolysis Stack  

SciTech Connect

An experimental study is under way to assess the performance of solid-oxide cells operating in the steam electrolysis mode for hydrogen production over a temperature range of 800 to 900C. Results presented in this paper were obtained from a ten-cell planar electrolysis stack, with an active area of 64 cm2 per cell. The electrolysis cells are electrolytesupported, with scandia-stabilized zirconia electrolytes (~140 m thick), nickel-cermet steam/hydrogen electrodes, and manganite air-side electrodes. The metallic interconnect plates are fabricated from ferritic stainless steel. The experiments were performed over a range of steam inlet mole fractions (0.1 - 0.6), gas flow rates (1000 - 4000 sccm), and current densities (0 to 0.38 A/cm2). Steam consumption rates associated with electrolysis were measured directly using inlet and outlet dewpoint instrumentation. Cell operating potentials and cell current were varied using a programmable power supply. Hydrogen production rates up to 100 Normal liters per hour were demonstrated. Values of area-specific resistance and stack internal temperatures are presented as a function of current density. Stack performance is shown to be dependent on inlet steam flow rate.

James O'Brien; Carl Stoots; Steve Herring; J. Hartvigsen

2005-05-01T23:59:59.000Z

420

Hydrogen program overview  

SciTech Connect

This paper consists of viewgraphs which summarize the following: Hydrogen program structure; Goals for hydrogen production research; Goals for hydrogen storage and utilization research; Technology validation; DOE technology validation activities supporting hydrogen pathways; Near-term opportunities for hydrogen; Market for hydrogen; and List of solicitation awards. It is concluded that a full transition toward a hydrogen economy can begin in the next decade.

Gronich, S. [Dept. of Energy, Washington, DC (United States). Office of Utility Technologies

1997-12-31T23:59:59.000Z

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


421

Critical Updates to the Hydrogen Analysis Production Model (H2A v3)  

NLE Websites -- All DOE Office Websites (Extended Search)

Critical Updates to the Hydrogen Critical Updates to the Hydrogen Analysis Production Model (H2A v3) Darlene Steward NREL Thursday, February 9, 2012 3:00 PM - 4:30 PM EST Darlene.steward@nrel.gov (303) 275 3837 NREL/PR-5600-54276 NATIONAL RENEWABLE ENERGY LABORATORY Outline 2 Introduction - Sara Dillich Overview of the H2A Model H2A Version 3 Changes Case Study Walkthrough Resources 1 2 3 4 NATIONAL RENEWABLE ENERGY LABORATORY Outline 3 Introduction - Sara Dillich Overview of the H2A Model H2A Version 3 Changes Case Study Walkthrough Resources 1 2 3 4 NATIONAL RENEWABLE ENERGY LABORATORY Overview of H2A Model 4 H2A Model Structure Getting Around Key Worksheets Do's and Don'ts - Do * Enter values in orange cells * Use the light green cells for notes and side calculations

422

Process and apparatus for the production of hydrogen by steam reforming of hydrocarbon  

DOE Patents (OSTI)

In the steam reforming of hydrocarbon, particularly methane, under elevated temperature and pressure to produce hydrogen, a feed of steam and hydrocarbon is fed into a first reaction volume containing essentially only reforming catalyst to partially reform the feed. The balance of the feed and the reaction products of carbon dioxide and hydrogen are then fed into a second reaction volume containing a mixture of catalyst and adsorbent which removes the carbon dioxide from the reaction zone as it is formed. The process is conducted in a cycle which includes these reactions followed by countercurrent depressurization and purge of the adsorbent to regenerate it and repressurization of the reaction volumes preparatory to repeating the reaction-sorption phase of the cycle.

Sircar, Shivaji (Wescosville, PA); Hufton, Jeffrey Raymond (Fogelsville, PA); Nataraj, Shankar (Allentown, PA)

2000-01-01T23:59:59.000Z

423

Hydrogen Production for Fuel Cells Via Reforming Coal-Derived Methanol  

SciTech Connect

Hydrogen can be produced from many feed stocks including coal. The objectives of this project are to establish and prove a hydrogen production pathway from coal-derived methanol for fuel cell applications. This progress report is the third report submitted to the DOE reporting on the status and progress made during the course of the project. This report covers the time period of April 1-June 30, 2004. This quarter saw progress in five areas. These areas are: (1) External evaluation of coal based methanol and the fuel cell grade baseline fuel, (2) Design, set up and initial testing of the autothermal reactor, (3) Experiments to determine the axial and radial thermal profiles of the steam reformers, (4) Catalyst degradation studies, and (5) Experimental investigations of heat and mass transfer enhancement methods by flow field manipulation. All of the projects are proceeding on or slightly ahead of schedule.

Paul A. Erickson

2004-06-30T23:59:59.000Z

424

Hydrogen Production for Fuel Cells Via Reforming Coal-Derived Methanol  

SciTech Connect

Hydrogen can be produced from many feedstocks including coal. The objectives of this project are to establish and prove a hydrogen production pathway from coal-derived methanol for fuel cell applications. This progress report is the seventh report submitted to the DOE reporting on the status and progress made during the course of the project. This report covers the time period of April 1-June 31, 2005. This quarter saw progress in these areas. These areas are: (1) Steam reformer transient response, (2) Heat transfer enhancement, (3) Catalyst degradation, (4) Catalyst degradation with bluff bodies, and (5) Autothermal reforming of coal-derived methanol. All of the projects are proceeding on or slightly ahead of schedule.

Paul A. Erickson

2005-06-30T23:59:59.000Z

425

HYDROGEN PRODUCTION FOR FUEL CELLS VIA REFORMING COAL-DERIVED METHANOL  

SciTech Connect

Hydrogen can be produced from many feed stocks including coal. The objectives of this project are to establish and prove a hydrogen production pathway from coal-derived methanol for fuel cell applications. This progress report is the second report submitted to the DOE reporting on the status and progress made during the course of the project. This report covers the time period of January 1--March 31, 2004. This quarter saw progress in five areas. These areas are: (1) Internal and external evaluations of coal based methanol and the fuel cell grade baseline fuel; (2) Experimental investigations of heat and mass transfer enhancement methods by flow field manipulation; (3) Design and set up of the autothermal reactor; (4) Steam reformation of Coal Based Methanol; and (5) Initial catalyst degradation studies. All of the projects are proceeding on or slightly ahead of schedule.

Paul A. Erickson

2004-04-01T23:59:59.000Z

426

Enhanced Hydrogen Production Integrated with CO2 Separation in a Single-Stage Reactor  

SciTech Connect

Hydrogen production from coal gasification can be enhanced by driving the equilibrium limited Water Gas Shift reaction forward by incessantly removing the CO{sub 2} by-product via the carbonation of calcium oxide. This project aims at using the OSU patented high-reactivity mesoporous precipitated calcium carbonate sorbent for removing the CO{sub 2} product. Preliminary experiments demonstrate the show the superior performance of the PCC sorbent over other naturally occurring calcium sorbents. Gas composition analyses show the formation of 100% pure hydrogen. Novel calcination techniques could lead to smaller reactor footprint and single-stage reactors that can achieve maximum theoretical H{sub 2} production for multicyclic applications. Sub-atmospheric calcination studies reveal the effect of vacuum level, diluent gas flow rate, thermal properties of the diluent gas and the sorbent loading on the calcination kinetics which play an important role on the sorbent morphology. Steam, which can be easily separated from CO{sub 2}, is envisioned to be a potential diluent gas due to its enhanced thermal properties. Steam calcination studies at 700-850 C reveal improved sorbent morphology over regular nitrogen calcination. A mixture of 80% steam and 20% CO{sub 2} at ambient pressure was used to calcine the spent sorbent at 820 C thus lowering the calcination temperature. Regeneration of calcium sulfide to calcium carbonate was achieved by carbonating the calcium sulfide slurry by bubbling CO{sub 2} gas at room temperature.

Mahesh Iyer; Himanshu Gupta; Danny Wong; Liang-Shih Fan

2005-09-30T23:59:59.000Z

427

Cold End Inserts for Process Gas Waste Heat Boilers Air Products, operates hydrogen production plants, which utilize large waste heat boilers (WHB)  

E-Print Network (OSTI)

Cold End Inserts for Process Gas Waste Heat Boilers Overview Air Products, operates hydrogen walls. Air Products tasked our team to design an insert to place in the tubes of the WHB to increase flow velocity, thereby reducing fouling of the WHB. Objectives Air Products wishes that our team

Demirel, Melik C.

428

Summary of research on hydrogen production from fossil fuels conducted at NETL  

SciTech Connect

In this presentation we will summarize the work performed at NETL on the production of hydrogen via partial oxidation/dry reforming of methane and catalytic decomposition of hydrogen sulfide. We have determined that high pressure resulted in greater carbon formation on the reforming catalysts, lower methane and CO2 conversions, as well as a H2/CO ratio. The results also showed that Rh/alumina catalyst is the most resistant toward carbon deposition both at lower and at higher pressures. We studied the catalytic partial oxidation of methane over Ni-MgO solid solutions supported on metal foams and the results showed that the foam-supported catalysts reach near-equilibrium conversions of methane and H2/CO selectivities. The rates of carbon deposition differ greatly among the catalysts, varying from 0.24 mg C/g cat h for the dipped foams to 7.0 mg C/g cat h for the powder-coated foams, suggesting that the exposed Cr on all of the foam samples may interact with the Ni-MgO catalyst to kinetically limit carbon formation. Effects of sulfur poisoning on reforming catalysts were studies and pulse sulfidation of catalyst appeared to be reversible for some of the catalysts but not for all. Under pulse sulfidation conditions, the 0.5%Rh/alumina and NiMg2Ox-1100C (solid solution) catalysts were fully regenerated after reduction with hydrogen. Rh catalyst showed the best overall activity, less carbon deposition, both fresh and when it was exposed to pulses of H2S. Sulfidation under steady state conditions significantly reduced catalyst activity. Decomposition of hydrogen sulfide into hydrogen and sulfur was studied over several supported metal oxides and metal oxide catalysts at a temperature range of 650-850C. H2S conversions and effective activation energies were estimated using Arrhenius plots. The results of these studies will further our understanding of catalytic reactions and may help in developing better and robust catalysts for the production of hydrogen from fossil fuels

Shamsi, Abolghasem

2008-03-30T23:59:59.000Z

429

Hydrogen Cryomagnetics  

E-Print Network (OSTI)

% cryogenics (inc. MRI) 29% pressurisation and purging 11%controlled atmospheres (inc. breathing) 6% 4 Figure 5. Simplified price-cost, supply-demand relationship that is central to the helium market model developed during the Helium Resources... of hydrogen large amounts of hydrogen must be available for liquefaction. This poses problems for the production of liquid hydrogen via intermittent wind energy and via microwave plasma reactors that are not scalable as a result of low hydrogen production...

Glowacki, B. A.; Hanely, E.; Nuttall, W. J.

2014-01-01T23:59:59.000Z

430

Ocean thermal plantships for production of ammonia as the hydrogen carrier.  

SciTech Connect

Conventional petroleum, natural gas, and coal are the primary sources of energy that have underpinned modern civilization. Their continued availability in the projected quantities required and the impacts of emission of greenhouse gases (GHGs) on the environment are issues at the forefront of world concerns. New primary sources of energy are being sought that would significantly reduce the emissions of GHGs. One such primary source that can help supply energy, water, and fertilizer without GHG emissions is available in the heretofore unexploited thermal gradients of the tropical oceans. The world's oceans are the largest natural collector and reservoir of solar energy. The potential of ocean energy is limitless for producing base-load electric power or ammonia as the hydrogen carrier and fresh water from seawater. However, until now, ocean energy has been virtually untapped. The general perception is that ocean thermal energy is limited to tropical countries. Therefore, the full potential of at-sea production of (1) ammonia as a hydrogen carrier and (2) desalinated water has not been adequately evaluated. Using ocean thermal plantships for the at-sea co-production of ammonia as a hydrogen carrier and desalinated water offer potential energy, environmental, and economic benefits that support the development of the technology. The introduction of a new widespread solution to our projected energy supply requires lead times of a decade or more. Although continuation of the ocean thermal program from the 1970s would likely have put us in a mitigating position in the early 2000s, we still have a window of opportunity to dedicate some of our conventional energy sources to the development of this renewable energy by the time new sources would be critically needed. The primary objective of this project is to evaluate the technical and economic viability of ocean thermal plantships for the production of ammonia as the hydrogen carrier. This objective is achieved by completing project tasks that consist of updating the John Hopkins University/Applied Physics Laboratory (JHU/APL) pilot plantship design and extrapolating it to commercial plantships, evaluating a new energy-efficient ammonia synthesis process, evaluating the co-production of desalinated water on plantships, and developing a conceptual design of a satellite plantships system for commercial-scale ammonia production. In addition, an industrial workshop was organized to present the results and develop future goals for commercialization of ocean thermal plantships by 2015. The following goals, arranged in chronological order, were examined at the workshop: (1) Global displacement of petroleum-fuel-based (diesel, fuel oil, naphtha) power generation for freeing up these fuels for transportation, chemical feedstock, and other high-valued uses; (2) At-sea production of desalinated water for regions of critical water shortages; (3) Displacement of carbon-based feed stocks and energy for production of ammonia fertilizers; (4) Development of hydrogen supply to allow economic processing of heavy crude oils and upgrading oil sands; (5) Development of ammonia-fueled distributed energy to displace natural-gas fueled power generation to free up natural gas for higher-value uses and the mitigation of issues associated with imported liquefied natural gas (LNG); and (6) Use of ammonia as a hydrogen carrier for transportation.

Panchal, C.B.; Pandolfini, P. P.; Kumm, W. H.; Energy Systems; Johns Hopkins Univ.; Arctic Energies, Ltd.

2009-12-02T23:59:59.000Z

431

Technical and Economic Assessment of Regional Hydrogen Transition Strategies  

E-Print Network (OSTI)

system spatial layouts for hydrogen production and deliveryWe estimate costs for hydrogen production, delivery anda hydrogen depot (i.e. hydrogen production facility or city-

Ogden, Joan; Yang, Christopher; Nicholas, Michael

2007-01-01T23:59:59.000Z

432

Experimental results of hydrogen distillation at the low power cryogenic column for the production of deuterium depleted hydrogen  

SciTech Connect

The Deuterium Removal Unit (DRU) has been designed and built at the Petersburg Nuclear Physics Inst. (PNPI) to produce isotopically pure hydrogen with deuterium content less than 1 ppm. The cryogenic distillation column of 2.2 cm inner diameter and 155 cm packing height is the main element of the DRU. Column performances at different hydrogen distillation operating modes have been measured. The height equivalent to theoretical plate (HETP) for the column is 2.2 cm and almost constant over a wide range of vapour flow rates. Deuterium depleted hydrogen with a deuterium content of less than 0.1 ppm was produced in required quantity. (authors)

Alekseev, I.; Fedorchenko, O.; Kravtsov, P.; Vasilyev, A.; Vznuzdaev, M. [Petersburg Nuclear Physics Inst., Leningrad district, Gatchina, 188300 (Russian Federation)

2008-07-15T23:59:59.000Z

433

Metabolic engineering of Caldicellulosiruptor bescii yields increased hydrogen production from lignocellulosic biomass  

SciTech Connect

Background: Members of the anaerobic thermophilic bacterial genus Caldicellulosiruptor are emerging candidates for consolidated bioprocessing (CBP) because they are capable of efficiently growing on biomass without conventional pretreatment. C. bescii produces primarily lactate, acetate and hydrogen as fermentation products, and while some Caldicellulosiruptor strains produce small amounts of ethanol C. bescii does not, making it an attractive background to examine the effects of metabolic engineering. The recent development of methods for genetic manipulation has set the stage for rational engineering of this genus for improved biofuel production. Here, we report the first targeted gene deletion, the gene encoding lactate dehydrogenase (ldh), for metabolic engineering of a member of this genus. Results: A deletion of the C. bescii L-lactate dehydrogenase gene (ldh) was constructed on a non-replicating plasmid and introduced into the C. bescii chromosome by marker replacement. The resulting strain failed to produce detectable levels of lactate from cellobiose and maltose, instead increasing production of acetate and H2 by 21-34% relative to the wild type and pyrFA parent strains. The same phenotype was observed on a real-world substrate switchgrass (Panicum virgatum). Furthermore, the ldh deletion strain grew to a higher maximum optical density than the wild type on maltose and cellobiose, consistent with the prediction that the mutant would gain additional ATP with increased acetate production. Conclusions: Deletion of ldh in C. bescii is the first use of recently developed genetic methods for metabolic engineering of these bacteria. This deletion resulted in a redirection of electron flow from production of lactate to acetate and hydrogen. New capabilities in metabolic engineering combined with intrinsic utilization of lignocellulosic materials position these organisms to provide a new paradigm for consolidated bioprocessing of fuels and other products from biomass.

Cha, Minseok [University of Georgia, Athens, GA; Chung, Daehwan [University of Georgia, Athens, GA; Elkins, James G [ORNL; Guss, Adam M [ORNL; Westpheling, Janet [University of Georgia, Athens, GA

2013-01-01T23:59:59.000Z

434

Electrokinetic Hydrogen Generation from Liquid Water Microjets  

E-Print Network (OSTI)

Electrochemical hydrogen production methods are quiteonly causative hydrogen production method. Although the massa method for the production of molecular hydrogen from

Duffin, Andrew M.; Saykally, Richard J.

2007-01-01T23:59:59.000Z

435

Electrokinetic Hydrogen Generation from Liquid Water Microjets  

E-Print Network (OSTI)

currents and hydrogen production rates are shown to followmolecules. The hydrogen production efficiency is currentlycurrently available hydrogen production routes that can be

Duffin, Andrew M.; Saykally, Richard J.

2007-01-01T23:59:59.000Z

436

Hydrogen refueling station costs in Shanghai  

E-Print Network (OSTI)

pieces of hardware: 1. Hydrogen production equipment (e.g.when evaluating hydrogen production costs. Many analyses inrespect to size and hydrogen production method. These costs

Weinert, Jonathan X.; Shaojun, Liu; Ogden, Joan M; Jianxin, Ma

2007-01-01T23:59:59.000Z

437

Project Information Form Project Title The Development of Lifecycle Data for Hydrogen Fuel Production and  

E-Print Network (OSTI)

Project Information Form Project Title The Development of Lifecycle Data for Hydrogen Fuel will be technologies and fuels related to renewable hydrogen. The literature review will produce a set of hydrogen hydrogen or hydrogen produced with technologies or fuels not currently in the LCFS. The study will assess

California at Davis, University of

438

Metallic Membrane Materials Development for Hydrogen Production from Coal Derived Syngas  

SciTech Connect

The goals of Office of Clean Coal are: (1) Improved energy security; (2) Reduced green house gas emissions; (3) High tech job creation; and (4) Reduced energy costs. The goals of the Hydrogen from Coal Program are: (1) Prove the feasibility of a 40% efficient, near zero emissions IGCC plant that uses membrane separation technology and other advanced technologies to reduce the cost of electricity by at least 35%; and (2) Develop H{sub 2} production and processing technologies that will contribute {approx}3% in improved efficiency and 12% reduction in cost of electricity.

O.N. Dogan; B.H. Howard; D.E. Alman

2012-02-26T23:59:59.000Z

439

RECENT ADVANCES IN THE DEVELOPMENT OF THE HYBRID SULFUR PROCESS FOR HYDROGEN PRODUCTION  

SciTech Connect

Thermochemical processes are being developed to provide global-scale quantities of hydrogen. A variant on sulfur-based thermochemical cycles is the Hybrid Sulfur (HyS) Process, which uses a sulfur dioxide depolarized electrolyzer (SDE) to produce the hydrogen. In the HyS Process, sulfur dioxide is oxidized in the presence of water at the electrolyzer anode to produce sulfuric acid and protons. The protons are transported through a cation-exchange membrane electrolyte to the cathode and are reduced to form hydrogen. In the second stage of the process, the sulfuric acid by-product from the electrolyzer is thermally decomposed at high temperature to produce sulfur dioxide and oxygen. The two gases are separated and the sulfur dioxide recycled to the electrolyzer for oxidation. The Savannah River National Laboratory (SRNL) has been exploring a fuel-cell design concept for the SDE using an anolyte feed comprised of concentrated sulfuric acid saturated with sulfur dioxide. The advantages of this design concept include high electrochemical efficiency and small footprint compared to a parallel-plate electrolyzer design. This paper will provide a summary of recent advances in the development of the SDE for the HyS process.

Hobbs, D.

2010-07-22T23:59:59.000Z

440

An on sun parametric study of solar hydrogen production using WO{sub 3} photoanodes  

SciTech Connect

The solar production of hydrogen using photoactive electrodes is a topic receiving much attention in recent years. The use of thin metal oxide films as photoanodes allows the water splitting reaction to occur at a much lower applied voltage than would be necessary with a straight electrolysis process. The University of Nevada Las Vegas in collaboration with the UK based firm Hydrogen Solar and funded by the United States Department of Energy, has developed a prototype of this type of cell using a WO{sub 3} photoanode. An on-sun test facility has been constructed by the UNLV Center for Energy Research (CER) where a study is being conducted with regard to the effects various design parameters on the rate of hydrogen evolution. Parameters being studied include electrolyte temperature, electrolyte flow rate, electrolyte resistivity, applied voltage, and membrane to electrode spacing. The data collected is used in a parametric study of the cell performance. The results of this study are then used to establish general trends as to the effects of these parameters on the performance of the cells outside of a laboratory environment. (author)

Halford, Christopher K. [UNLV Center for Energy Research, 4505 S. Maryland Parkway, Las Vegas, NV 89154 (United States); Boehm, Robert F. [UNLV Center for Energy Research, 4505 S. Maryland Parkway, UNLV Box 454027, Las Vegas, NV 89154-4027 (United States)

2011-01-15T23:59:59.000Z

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


441

HYDROGEN PRODUCTION FOR FUEL CELLS VIA REFORMING COAL-DERIVED METHANOL  

SciTech Connect

Hydrogen can be produced from many feed stocks including coal. The objectives of this project are to establish and prove a hydrogen production pathway from coal-derived methanol for fuel cell applications. This progress report is the first such report that will be submitted to the DOE reporting on the status and progress made during the course of the project. This report covers the time period of October 1--December 31, 2003. This quarter saw progress in three areas. These areas are: (1) Evaluations of coal based methanol and the fuel cell grade baseline fuel, (2) Design and set up of the autothermal reactor, as well as (3) Set up and data collection of baseline performance using the steam reformer. All of the projects are proceeding on schedule. During this quarter one conference paper was written that will be presented at the ASME Power 2004 conference in March 2004, which outlines the research direction and basis for looking at the coal to hydrogen pathway.

Paul A. Erickson

2004-04-01T23:59:59.000Z

442

Hydrogen Production for Fuel Cells Via Reforming Coal-Derived Methanol  

SciTech Connect

Hydrogen can be produced from many feed stocks including coal. The objectives of this project are to establish and prove a hydrogen production pathway from coal-derived methanol for fuel cell applications. This progress report is the fourth report submitted to the DOE reporting on the status and progress made during the course of the project. This report covers the time period of July 1-Sept 30, 2004 along with a recap of progress from the start of the project on Oct 1, 2003 to Sept 30, 2004. All of the projects are proceeding on or slightly ahead of schedule. This year saw progress in several areas. These areas are: (1) External and internal evaluation of coal based methanol and a fuel cell grade baseline fuel, (2) Design set up and initial testing of three laboratory scale steam reformers, (3) Design, set up and initial testing of a laboratory scale autothermal reactor, (4) Hydrogen generation from coal-derived methanol using steam reformation, (5) Experiments to determine the axial and radial thermal profiles of the steam reformers, (6) Initial catalyst degradation studies with steam reformation and coal based methanol, and (7) Experimental investigations of heat and mass transfer enhancement methods by flow field manipulation. All of the projects are proceeding on or slightly ahead of schedule.

Paul A. Erickson

2004-09-30T23:59:59.000Z

443

Solar photocatalytic hydrogen production from water using a dual bed photosystem. Task 2 report; Annual report  

SciTech Connect

This work is an investigation into the use of photocatalytic particles in a dual bed configuration, so as to effect the solar-driven decomposition of water to its constituent elements, particularly hydrogen. The system envisioned would consist of two modules, each consisting of a shallow, flat, sealed container, in which micron-sized photocatalytic particles are immobilized. An aqueous solution containing a redox mediator is pumped between the two chambers. Different photoparticles and catalysts are chosen for their respective modules so as to effect oxidative water-splitting in one vessel to evolve oxygen gas, and reductive water-splitting in the other to evolve hydrogen. This is a direct photoconversion scheme that breaks down the energetic requirement for water decomposition into a 2-photon process, and enables separate production of hydrogen and oxygen. Titanium dioxide, TiO{sub 2}, and indium phosphide, InP, were employed as photoparticles in the O{sub 2}- and H{sub 2}-evolving beds, respectively. Platinum catalysts were evaluated to prompt H{sub 2}-evolution. Calculations on the energy band structure of free and immobilized particles provided guidance as to how the microstructure of the particles should be configured. A series of redox mediators, spanning a range of redox potentials, were tested. While many electron donors facilitated H{sub 2}-evolution, only the most oxidizing ones enabled O{sub 2}-evolution. A single redox couple, capable of charge exchange in both modules, is desirable to avoid system design complexity.

Linkous, C.A.; McKaige, G.T.; Slattery, D.K.; Ouellette, A.J.A.; Austin, B.C.N.

1995-12-01T23:59:59.000Z

444

Maintaining a Technology-Neutral Approach to Hydrogen Production Process Development through Conceptual Design of the Next Generation Nuclear Plant  

SciTech Connect

The Next Generation Nuclear Plant (NGNP) project was authorized in the Energy Policy Act of 2005 (EPAct), tasking the U.S. Department of Energy (DOE) with demonstrating High Temperature Gas-Cooled Reactor (HTGR) technology. The demonstration is to include the technical, licensing, operational, and commercial viability of HTGR technology for the production of electricity and hydrogen. The Nuclear Hydrogen Initiative (NHI), a component of the DOE Hydrogen Program managed by the Office of Nuclear Energy, is also investigating multiple approaches to cost effective hydrogen production from nuclear energy. The objective of NHI is development of the technology and information basis for a future decision on commercial viability. The initiatives are clearly intertwined. While the objectives of NGNP and NHI are generally consistent, NGNP has progressed to the project definition phase and the project plan has matured. Multiple process applications for the NGNP require process heat, electricity and hydrogen in varied combinations and sizes. Coupling these processes to the reactor in multiple configurations adds complexity to the design, licensing and demonstration of both the reactor and the hydrogen production process. Commercial viability of hydrogen production may depend on the specific application and heat transport configuration. A component test facility (CTF) is planned by the NGNP to support testing and demonstration of NGNP systems, including those for hydrogen production, in multiple configurations. Engineering-scale demonstrations in the CTF are expected to start in 2012 to support scheduled design and licensing activities leading to subsequent construction and operation. Engineering-scale demonstrations planned by NHI are expected to start at least two years later. Reconciliation of these schedules is recommended to successfully complete both initiatives. Hence, closer and earlier integration of hydrogen process development and heat transport systems is sensible. For integration purposes, an analysis comparing the design, cost and schedule impact of maintaining a technology neutral approach through conceptual design or making an early hydrogen process technology selection was performed. Early selection does not specifically eliminate a technology, but rather selects the first hydrogen technology for demonstration. A systems-engineering approach was taken to define decision-making criteria for selecting a hydrogen technology. The relative technical, cost and schedule risks of each approach were analyzed and risk mitigation strategies were recommended, including provisions to maintain close collaboration with the NHI. The results of these analyses are presented here.

Michael W. Patterson

2008-05-01T23:59:59.000Z

445

Effects of pretreatment method of natural bacteria source on microbial community and bio-hydrogen production by dark fermentation  

Science Journals Connector (OSTI)

The effects of pretreatment method of cow dung compost, which was employed as natural hydrogen bacteria source, on the microbial community, population distribution of microbes and hydrogen production potential were investigated in the batch tests. The maximum hydrogen yield of 290.8mL/L-culture appeared in the pretreated method A (infrared drying) by dark fermentation. The pretreated method of compost significantly affected microbial succession, population distribution of microbes. Both Clostridium sp. and Enterobacter sp. were found to be two species of preponderant hydrogen-producing bacteria, the next best was Bacteroides sp. and Veillonella sp., the last was Lactobacillus sp. and Streptococcus sp., which were also essential. The results showed that the mutualism and symbiosis relations of the mixed bacteria played a critical role in hydrogen fermentation process.

Zhao-Xia Song; Yang Dai; Qi-Long Fan; Xiao-Hu Li; Yao-Ting Fan; Hong-Wei Hou

2012-01-01T23:59:59.000Z

446

Economic Analysis of Production and Use of Hydrogen From Solar Energy, Wind, Hydropower and Biomass  

Science Journals Connector (OSTI)

In the vision of global hydrogen economy, hydrogen produced with renewable energy is seen as one of the cleanest final energy carriers.

Amela Ajanovic; Reinhard Haas

2009-01-01T23:59:59.000Z

447

Economic Analysis of Various Reforming Techniques and Fuel Sources for Hydrogen Production.  

E-Print Network (OSTI)

??Hydrogen is emerging as a future replacement fuel for the traditional fossil fuels that will be capable of satisfying our energy needs. Hydrogen may enable (more)

MCGLOCKLIN, KRISTIN

2006-01-01T23:59:59.000Z

448

BIMETALLIC NANOCATALYSTS IN MESOPOROUS SILICA FOR HYDROGEN PRODUCTION FROM COAL-DERIVED FUELS  

SciTech Connect

In steam reforming reactions (SRRs) of alkanes and alcohols to produce H{sub 2}, noble metals such as platinum (Pt) and palladium (Pd) are extensively used as catalyst. These metals are expensive; so, to reduce noble-metal loading, bi-metallic nanocatalysts containing non-noble metals in MCM-41 (Mobil Composition of Material No. 41, a mesoporous material) as a support material with high-surface area were synthesized using one-pot hydrothermal procedure with a surfactant such as cetyltrimethylammonium bromide (CTAB) as a template. Bi-metallic nanocatalysts of Pd-Ni and Pd-Co with varying metal loadings in MCM-41 were characterized by x-ray diffraction (XRD), N{sub 2} adsorption, and Transmission electron microscopy (TEM) techniques. The BET surface area of MCM-41 (~1000 m{sup 2}/g) containing metal nanoparticles decreases with the increase in metal loading. The FTIR studies confirm strong interaction between Si-O-M (M = Pd, Ni, Co) units and successful inclusion of metal into the mesoporous silica matrix. The catalyst activities were examined in steam reforming of methanol (SRM) reactions to produce hydrogen. Reference tests using catalysts containing individual metals (Pd, Ni and Co) were also performed to investigate the effect of the bimetallic system on the catalytic behavior in the SRM reactions. The bimetallic system remarkably improves the hydrogen selectivity, methanol conversion and stability of the catalyst. The results are consistent with a synergistic behavior for the Pd-Ni-bimetallic system. The performance, durability and thermal stability of the Pd-Ni/MCM-41 and Pd-Co/MCM-41 suggest that these materials may be promising catalysts for hydrogen production from biofuels. A part of this work for synthesis and characterization of Pd-Ni-MCM-41 and its activity for SRM reactions has been published (Development of Mesoporous Silica Encapsulated Pd-Ni Nanocatalyst for Hydrogen Production in Production and Purification of Ultraclean Transportation Fuels; Hu, Y., et al.; ACS Symposium Series; American Chemical Society: Washington, DC, 2011.)

Kuila, Debasish; Ilias, Shamsuddin

2013-02-13T23:59:59.000Z

449

PROGRESS IN HIGH-TEMPERATURE ELECTROLYSIS FOR HYDROGEN PRODUCTION USING PLANAR SOFC TECHNOLOGY  

SciTech Connect

A research program is under way at the Idaho National Laboratory to assess the performance of solid-oxide cells operating in the steam electrolysis mode for hydrogen production over a temperature range of 800 to 900C. The research program includes both experimental and modeling activities. Selected results from both activities are presented in this paper. Experimental results were obtained from a ten-cell planar electrolysis stack, fabricated by Ceramatec , Inc. The electrolysis cells are electrolyte-supported, with scandia-stabilized zirconia electrolytes (~140 m thick), nickel-cermet steam/hydrogen electrodes, and manganite air-side electrodes. The metallic interconnect plates are fabricated from ferritic stainless steel. The experiments were performed over a range of steam inlet mole fractions (0.1 - 0.6), gas flow rates (1000 - 4000 sccm), and current densities (0 to 0.38 A/cm2). Hydrogen production rates up to 90 Normal liters per hour were demonstrated. Stack performance is shown to be dependent on inlet steam flow rate. A three-dimensional computational fluid dynamics (CFD) model was also created to model high-temperature steam electrolysis in a planar solid oxide electrolysis cell (SOEC). The model represents a single cell as it would exist in the experimental electrolysis stack. Mass, momentum, energy, and species conservation and transport are provided via the core features of the commercial CFD code FLUENT1. A solid-oxide fuel cell (SOFC) model adds the electrochemical reactions and loss mechanisms and computation of the electric field throughout the cell. The FLUENT SOFC user-defined subroutine was modified for this work to allow for operation in the SOEC mode. Model results provide detailed profiles of temperature, Nernst potential, operating potential, anode-side gas composition, cathode-side gas composition, current density and hydrogen production over a range of stack operating conditions. Mean model results are shown to compare favorably with the experimental results obtained from the ten-cell stack tested at INL.

O'Brien, J. E.; Herring, J. S.; Stoots, C. M.; Hawkes, G. L.; Hartvigsen, J., J.; Mehrdad Shahnam

2005-04-01T23:59:59.000Z

450

Hydrogen production from an ethanol reformer with energy saving approaches over various catalysts  

Science Journals Connector (OSTI)

The reforming of ethanol for hydrogen production was carried out in this study. The effects of ethanol supply rate, catalysts, O2/EtOH and different energy-saving approaches on the reforming temperature, H2+CO (syngas) concentration and thermal efficiency were investigated. The results showed that the best H2+CO concentration of 43.41% could be achieved by using rhodium (Rh), while the next best concentration of about 42.08% could be obtained using ruthenium (Ru). The results also showed that the conversion efficiency of ethanol, concentrations of H2 and CO, and the energy loss ratio could be improved by heat insulation and heat recycling; and the improvement in the reforming performance was greater by the Ru catalyst rather than by the Rh catalyst with the energy-saving approaches. The greatest improvement in hydrogen production was achieved when using the Ru catalyst with the addition of steam and heat recycling system under an O2/EtOH ratio of 0.625 and S/C ratio of 1.0.

Wei-Cheng Chiu; Rong-Fang Horng; Huann-Ming Chou

2013-01-01T23:59:59.000Z

451

Hydrogen Production from Biomass-Derived Syngas Using a Membrane Reactor Based Process  

Science Journals Connector (OSTI)

(1) One of the benefits of adopting H2 as an energy source, in addition to reducing CO2 emissions, is that it can be produced from readily available and plentiful raw materials such as coal and renewable biomass; this then diminishes the need to use the worlds dwindling crude-oil resources. ... For that, coal must be first gasified with air or pure O2 at high temperatures(2) to produce coal-gasifier off-gas (or syngas), containing as key species H2, CO, CO2, H2O, CH4, and other byproducts such as organic vapors, tars, H2S, and NH3, etc.,(2) the exact composition depending on the operating conditions, e.g., pressure, temperature, type of coal and oxidant used and their flow rates, and gasifier configuration, etc.(2) ... A novel MR system termed as the one-box process, in which syngas cleanup, hydrogen production via the WGS reaction, and product separation are combined in the same unit, was successfully utilized for producing hydrogen from a feed with a simulated biomass-derived syngas containing common impurities such as H2S and NH3, a model organic vapor (toluene), and a model tar-like species (naphthalene). ...

Jiang Yu; Mingyang Tan; Paul K. T. Liu; Muhammad Sahimi; Theodore T. Tsotsis

2013-12-27T23:59:59.000Z

452

Novel, Magnetically Fluidized-Bed Reactor Development for the Looping Process: Coal to Hydrogen Production Research and Development  

NLE Websites -- All DOE Office Websites (Extended Search)

Novel, Magnetically Fluidized-Bed Novel, Magnetically Fluidized-Bed Reactor Development for the Looping Process: Coal to Hydrogen Production Research and Development Background The U.S. Department of Energy (DOE) National Energy Technology Laboratory (NETL) is committed to improving methods for co-producing power and chemicals, fuels, and hydrogen (H2). Gasification is a process by which fuels such as coal can be used to produce synthesis gas (syngas), a mixture of H2, carbon monoxide (CO), and carbon

453

Life cycle assessment of hydrogen production from S-I thermochemical process coupled to a high temperature gas reactor  

SciTech Connect

The purpose of this paper is to quantify the greenhouse gas (GHG) emissions associated to the hydrogen produced by the sulfur-iodine thermochemical process, coupled to a high temperature nuclear reactor, and to compare the results with other life cycle analysis (LCA) studies on hydrogen production technologies, both conventional and emerging. The LCA tool was used to quantify the impacts associated with climate change. The product system was defined by the following steps: (i) extraction and manufacturing of raw materials (upstream flows), (U) external energy supplied to the system, (iii) nuclear power plant, and (iv) hydrogen production plant. Particular attention was focused to those processes where there was limited information from literature about inventory data, as the TRISO fuel manufacture, and the production of iodine. The results show that the electric power, supplied to the hydrogen plant, is a sensitive parameter for GHG emissions. When the nuclear power plant supplied the electrical power, low GHG emissions were obtained. These results improve those reported by conventional hydrogen production methods, such as steam reforming. (authors)

Giraldi, M. R.; Francois, J. L.; Castro-Uriegas, D. [Departamento de Sistemas Energeticos, Facultad de Ingenieria, Universidad Nacional Autonoma de Mexico, Paseo Cuauhnahuac No. 8532, Col. Progreso, C.P. 62550, Jiutepec, Morelos (Mexico)

2012-07-01T23:59:59.000Z

454

NREL: Hydrogen and Fuel Cells Research - Hydrogen Storage  

NLE Websites -- All DOE Office Websites (Extended Search)

L. Simpson. (2010) Contact: Thomas Gennett 303-384-6628 Printable Version Hydrogen & Fuel Cells Research Home Projects Fuel Cells Hydrogen Production & Delivery Hydrogen Storage...

455

An Assessment of the Near-Term Costs of Hydrogen Refueling Stations and Station Components  

E-Print Network (OSTI)

Hydrogen Production .pieces of hardware: 1. Hydrogen production equipment (e.g.when evaluating hydrogen production costs and sales prices.

Weinert, Jonathan X.; Lipman, Timothy

2006-01-01T23:59:59.000Z

456

Production of hydrogen, liquid fuels, and chemicals from catalytic processing of bio-oils  

SciTech Connect

Disclosed herein is a method of generating hydrogen from a bio-oil, comprising hydrogenating a water-soluble fraction of the bio-oil with hydrogen in the presence of a hydrogenation catalyst, and reforming the water-soluble fraction by aqueous-phase reforming in the presence of a reforming catalyst, wherein hydrogen is generated by the reforming, and the amount of hydrogen generated is greater than that consumed by the hydrogenating. The method can further comprise hydrocracking or hydrotreating a lignin fraction of the bio-oil with hydrogen in the presence of a hydrocracking catalyst wherein the lignin fraction of bio-oil is obtained as a water-insoluble fraction from aqueous extraction of bio-oil. The hydrogen used in the hydrogenating and in the hydrocracking or hydrotreating can be generated by reforming the water-soluble fraction of bio-oil.

Huber, George W; Vispute, Tushar P; Routray, Kamalakanta

2014-06-03T23:59:59.000Z

457

LY294002 and LY303511 Sensitize Tumor Cells to Drug-Induced Apoptosis via Intracellular Hydrogen Peroxide Production Independent of the Phosphoinositide 3-Kinase-Akt Pathway  

Science Journals Connector (OSTI)

...oxygen species production, in particular hydrogen peroxide...intracellular H2O2 production and downstream...Materials and Methods Determination...Materials and Methods. The total...intracellular H2O2 production at a concentration...produces hydrogen peroxide...

Tze Wei Poh and Shazib Pervaiz

2005-07-15T23:59:59.000Z

458

Assessment of CO2 capture options from various points in steam methane reforming for hydrogen production  

Science Journals Connector (OSTI)

Abstract Steam methane reforming (SMR) is currently the main hydrogen production process in industry, but it has high emissions of CO2, at almost 7kg CO2/kg H2 on average, and is responsible for about 3% of global industrial sector CO2 emissions. Here, the results are reported of an investigation of the effect of steam-to-carbon ratio (S/C) on CO2 capture criteria from various locations in the process, i.e. synthesis gas stream (location 1), pressure swing adsorber (PSA) tail gas (location 2), and furnace flue gases (location 3). The CO2 capture criteria considered in this study are CO2 partial pressure, CO2 concentration, and CO2 mass ratio compared to the final exhaust stream, which is furnace flue gases. The CO2 capture number (Ncc) is proposed as measure of capture favourability, defined as the product of the three above capture criteria. A weighting of unity is used for each criterion. The best S/C ratio, in terms of providing better capture option, is determined. CO2 removal from synthesis gas after the shift unit is found to be the best location for CO2 capture due to its high partial pressure of CO2. However, furnace flue gases, containing almost 50% of the CO2 in produced in the process, are of great significance environmentally. Consequently, the effects of oxygen enrichment of the furnace feed are investigated, and it is found that this measure improves the CO2 capture conditions for lower S/C ratios. Consequently, for an S/C ratio of 2.5, CO2 capture from a flue gas stream is competitive with two other locations provided higher weighting factors are considered for the full presence of CO2 in the flue gases stream. Considering carbon removal from flue gases, the ratio of hydrogen production rate and Ncc increases with rising reformer temperature.

R. Soltani; M.A. Rosen; I. Dincer

2014-01-01T23:59:59.000Z

459

Enhanced Hydrogen Production Integrated with CO2 Separation in a Single-Stage  

SciTech Connect

Enhancement in the production of high purity hydrogen from fuel gas, obtained from coal gasification, is limited by thermodynamics of the Water Gas Shift Reaction. However, this constraint can be overcome by concurrent water-gas shift (WGS) and carbonation reactions to enhance H{sub 2} production by incessantly driving the equilibrium-limited WGS reaction forward and in-situ removing the CO2 product from the gas mixture. The spent sorbent is then regenerated by calcining it to produce a pure stream of CO{sub 2} and CaO which can be reused. However while performing the cyclic carbonation and calcination it was observed that the CO{sub 2} released during the in-situ calcination causes the deactivation of the iron oxide WGS catalyst. Detailed understanding of the iron oxide phase diagram helped in developing a catalyst pretreatment procedure using a H{sub 2}/H{sub 2}O system to convert the deactivated catalyst back to its active magnetite (Fe{sub 3}O{sub 4}) form. The water gas shift reaction was studied at different temperatures, different steam to carbon monoxide ratios (S/C) 3:1, 2:1, 1:1 and different total pressures ranging from 0-300 psig. The combined water gas shift and carbonation reaction was investigated at temperatures ranging from 600-700C, S/C ratio of 3:1 to 1:1 and at different pressures of 0-300 psig and the calcium looping process was found to produce high purity hydrogen with in-situ CO{sub 2} capture.

Mahesh Iyer; Shwetha Ramkumar; Liang-Shih Fan

2006-09-30T23:59:59.000Z

460

Efficient, sustainable production of molecular hydrogen -a promising alternative to batteries in terms of energy storage -is still an unsolved problem. Implementation of direct water splitting  

E-Print Network (OSTI)

in terms of energy storage - is still an unsolved problem. Implementation of direct water splitting usingEfficient, sustainable production of molecular hydrogen - a promising alternative to batteries

Ku?el, Petr

Note: This page contains sample records for the topic "hydrogen production cxs" from the National Library of EnergyBeta (NLEBeta).
While these samples are representative of the content of NLEBeta,
they are not comprehensive nor are they the most current set.
We encourage you to perform a real-time search of NLEBeta
to obtain the most current and comprehensive results.


461

X-ray Photoelectron Spectroscopy of GaP{1-x}N(x) Photocorroded as a Result of Hydrogen Production through Water Electrolysis  

E-Print Network (OSTI)

X-ray Photoelectron Spectroscopy of GaP{1-x}N(x) Photocorroded as a Result of Hydrogen Production through Water Electrolysis

Mayer, Marie A

2006-01-01T23:59:59.000Z

462

JOURNAL DE PHYSIQUE Colloque C6, suppliment au no 8, Tome 39, aolit 1978, page C6-108 A PROPOSED PRODUCTION METHOD FOR SPIN-ALIGNED HYDROGEN  

E-Print Network (OSTI)

PRODUCTION METHOD FOR SPIN-ALIGNED HYDROGEN William C. Stwalley, Univ. of Iowa, Iowa Citg, IA 52242, U.S. A (but thusfar hypothetical) substance, spin-aligned hydrogen, is described. INTRODUCTION.- Spin-aligned atoms of dominant current in- terest are the isotopes of spin-aligned hydrogen /2,3/. Only spin

Boyer, Edmond

463

A Novel Combustion Synthesis Preparation of CuO/ZnO/ZrO2/Pd for Oxidative Hydrogen Production from Methanol  

E-Print Network (OSTI)

cells using hydrogen as fuel are efficient, quiet, and have near zero harmful emissions. Elemental fuel cells that use precious metal catalysts such as platinum require hydrogen fuel which contains lessA Novel Combustion Synthesis Preparation of CuO/ZnO/ZrO2/Pd for Oxidative Hydrogen Production from

Mukasyan, Alexander

464

HIGH-TEMPERATURE ELECTROLYSIS FOR LARGE-SCALE HYDROGEN AND SYNGAS PRODUCTION FROM NUCLEAR ENERGY SYSTEM SIMULATION AND ECONOMICS  

SciTech Connect

A research and development program is under way at the Idaho National Laboratory (INL) to assess the technological and scale-up issues associated with the implementation of solid-oxide electrolysis cell technology for efficient high-temperature hydrogen production from steam. This work is supported by the US Department of Energy, Office of Nuclear Energy, under the Nuclear Hydrogen Initiative. This paper will provide an overview of large-scale system modeling results and economic analyses that have been completed to date. System analysis results have been obtained using the commercial code UniSim, augmented with a custom high-temperature electrolyzer module. Economic analysis results were based on the DOE H2A analysis methodology. The process flow diagrams for the system simulations include an advanced nuclear reactor as a source of high-temperature process heat, a power cycle and a coupled steam electrolysis loop. Several reactor types and power cycles have been considered, over a range of reactor outlet temperatures. Pure steam electrolysis for hydrogen production as well as coelectrolysis for syngas production from steam/carbon dioxide mixtures have both been considered. In addition, the feasibility of coupling the high-temperature electrolysis process to biomass and coal-based synthetic fuels production has been considered. These simulations demonstrate that the addition of supplementary nuclear hydrogen to synthetic fuels production from any carbon source minimizes emissions of carbon dioxide during the production process.

J. E. O'Brien; M. G. McKellar; E. A. Harvego; C. M. Stoots

2009-05-01T23:59:59.000Z

465

Plasma steam reforming of E85 for hydrogen rich gas production  

Science Journals Connector (OSTI)

E85 (85?vol% ethanol and 15?vol% gasoline) is a partly renewable fuel that is increasing in supply availability. Hydrogen production from E85 for fuel cell or internal combustion engine applications is a potential method for reducing CO2 emissions. Steam reforming of E85 using a nonthermal plasma (pulse corona discharge) reactor has been exploited at low temperature (200300?C) without external heating, diluent gas, oxidant or catalyst in this work. Several operational parameters, including the discharge current, E85 concentration and feed flow rate, have been investigated. The results show that hydrogen rich gases (6367% H2 and 2229% CO, with small amounts of CO2, C2 hydrocarbons and CH4) can be produced by this method. A comparison with ethanol reforming and gasoline reforming under identical conditions has also been made and the behaviour of E85 reforming is found to be close to that of ethanol reforming with slightly higher C2 hydrocarbons yields.

Xinli Zhu; Trung Hoang; Lance L Lobban; Richard G Mallinson

2011-01-01T23:59:59.000Z

466

Theoretical Design of Molecular Electrocatalysts with Flexible Pendant Amines for Hydrogen Production and Oxidation  

SciTech Connect

The design of hydrogen oxidation and production catalysts is important for the development of alternative renewable energy sources. The overall objective is to maximize the turnover frequency and minimize the overpotential. In an effort to assist in the design of such catalysts, we use computational methods to examine a variety of nickel-based molecular electrocatalysts with pendant amines. Our studies focus on the proton-coupled electron transfer (PCET) process involving electron transfer between the complex and the electrode and intramolecular proton transfer between the nickel center and the nitrogen of the pendant amine. The concerted PCET mechanism, which tends to require a lower overpotential, is favored by a smaller equilibrium Ni-N distance and a more flexible pendant amine ligand, thereby decreasing the energetic penalty for the nitrogen to approach the nickel center for proton transfer. These calculations provide design principles that will be useful for developing the next generation of hydrogen catalysts. This research was supported as part of the Center for Molecular Electrocatalysis, an Energy Frontier Research Center funded by the U. S. Department of Energy, Office of Science, Office of Basic Energy Sciences.

Fernandez, Laura; Horvath, Samantha; Hammes-Schiffer, Sharon

2013-02-07T23:59:59.000Z

467

Final LDRD report : metal oxide films, nanostructures, and heterostructures for solar hydrogen production.  

SciTech Connect

The distinction between electricity and fuel use in analyses of global power consumption statistics highlights the critical importance of establishing efficient synthesis techniques for solar fuels-those chemicals whose bond energies are obtained through conversion processes driven by solar energy. Photoelectrochemical (PEC) processes show potential for the production of solar fuels because of their demonstrated versatility in facilitating optoelectronic and chemical conversion processes. Tandem PEC-photovoltaic modular configurations for the generation of hydrogen from water and sunlight (solar water splitting) provide an opportunity to develop a low-cost and efficient energy conversion scheme. The critical component in devices of this type is the PEC photoelectrode, which must be optically absorptive, chemically stable, and possess the required electronic band alignment with the electrochemical scale for its charge carriers to have sufficient potential to drive the hydrogen and oxygen evolution reactions. After many decades of investigation, the primary technological obstacle remains the development of photoelectrode structures capable of efficient conversion of light with visible frequencies, which is abundant in the solar spectrum. Metal oxides represent one of the few material classes that can be made photoactive and remain stable to perform the required functions.

Kronawitter, Coleman X. [Lawrence Berkeley National Laboratory, Berkeley, CA; Antoun, Bonnie R.; Mao, Samuel S. [Lawrence Berkeley National Laboratory, Berkeley, CA

2012-01-01T23:59:59.000Z

468

Catalyst for Recombination of Hydrogen and Oxygen in Confined Spaces Under High Concentrations of Hydrogen  

Science Journals Connector (OSTI)

Technical Paper / Safety and Technology of Nuclear Hydrogen Production, Control, and Management / Hydrogen Safety and Recombiners

V. Shepelin; D. Koshmanov; E. Chepelin

469

Hydrogen & Fuel Cells - Hydrogen - Hydrogen Quality  

NLE Websites -- All DOE Office Websites (Extended Search)

Hydrogen Quality Issues for Fuel Cell Vehicles Hydrogen Quality Issues for Fuel Cell Vehicles Introduction Developing and implementing fuel quality specifications for hydrogen are prerequisites to the widespread deployment of hydrogen-fueled fuel cell vehicles. Several organizations are addressing this fuel quality issue, including the International Standards Organization (ISO), the Society of Automotive Engineers (SAE), the California Fuel Cell Partnership (CaFCP), and the New Energy and Industrial Technology Development Organization (NEDO)/Japan Automobile Research Institute (JARI). All of their activities, however, have focused on the deleterious effects of specific contaminants on the automotive fuel cell or on-board hydrogen storage systems. While it is possible for the energy industry to provide extremely pure hydrogen, such hydrogen could entail excessive costs. The objective of our task is to develop a process whereby the hydrogen quality requirements may be determined based on life-cycle costs of the complete hydrogen fuel cell vehicle "system." To accomplish this objective, the influence of different contaminants and their concentrations in fuel hydrogen on the life-cycle costs of hydrogen production, purification, use in fuel cells, and hydrogen analysis and quality verification are being assessed.

470

Nuclear Hydrogen Initiative  

NLE Websites -- All DOE Office Websites (Extended Search)

Advanced Nuclear Research Advanced Nuclear Research Office of Nuclear Energy, Science and Technology FY 2003 Programmatic Overview Nuclear Hydrogen Initiative Nuclear Hydrogen Initiative Office of Nuclear Energy, Science and Technology Henderson/2003 Hydrogen Initiative.ppt 2 Nuclear Hydrogen Initiative Nuclear Hydrogen Initiative Program Goal * Demonstrate the economic commercial-scale production of hydrogen using nuclear energy by 2015 Need for Nuclear Hydrogen * Hydrogen offers significant promise for reduced environmental impact of energy use, specifically in the transportation sector * The use of domestic energy sources to produce hydrogen reduces U.S. dependence on foreign oil and enhances national security * Existing hydrogen production methods are either inefficient or produce

471

Fermentation and Electrohydrogenic Approaches to Hydrogen Production - DOE Hydrogen and Fuel Cells Program FY 2012 Annual Progress Report  

NLE Websites -- All DOE Office Websites (Extended Search)

8 8 DOE Hydrogen and Fuel Cells Program FY 2012 Annual Progress Report Pin-Ching Maness (Primary Contact), Katherine Chou, and Lauren Magnusson National Renewable Energy Laboratory (NREL) 15013 Denver West Parkway Golden, CO 80401 Phone: (303) 384-6114 Email: pinching.maness@nrel.gov DOE Manager HQ: Eric Miller Phone: (202) 287-5829 Email: Eric.Miller@hq.doe.gov Subcontractor: Bruce Logan, Pennsylvania State University, State College, PA Start Date: October 1, 2004 Projected End Date: Project continuation and direction determined annually by DOE Fiscal Year (FY) 2012 Objectives Optimize sequencing fed-batch parameters in converting * cellulose to hydrogen by the cellulolytic bacterium Clostridium thermocellum; aimed at lowering feedstock cost. Improve plasmid stability in * C. thermocellum; aimed

472

Hydrogen Storage Technologies: Long-Term Commercialization Approach with First Products First  

NLE Websites -- All DOE Office Websites (Extended Search)

Technologies Technologies Long-term commercialization approach with first products first Hydrogen and Fuel Cell Technologies Manufacturing R&D Workshop Washington, DC Glenn Rambach August 11, 2011 Potential market area for fuel cells (or other power plants). Defined by peak power vs. cost per unit power capacity (W vs. $/kW) for typical applications currently satisfied by legacy technologies. Auto Transit bus 2-cycle scooter Portable generator Wheelchair Fork lift Telecom backup Strategic portable Educational device Retail A Less difficult Less difficult (smaller units) (cost tolerant market) Auto Transit bus 2-cycle scooter Portable generator Wheelchair Fork lift Telecom backup Strategic portable Educational device Retail A Range of application size and specific cost that all can be commercially satisfied

473

Techno-Economic Boundary Analysis of Biological Pathways to Hydrogen Production (2009)  

NLE Websites -- All DOE Office Websites (Extended Search)

September 2013 September 2013 Presentation to: Biological Hydrogen Production Workshop By: Brian D. James Strategic Analysis Inc. Bjames@sainc.com (703) 778-7114 1 This presentation does not contain any proprietary, confidential, or otherwise restricted information * DOE/NREL Bio H 2 Working Group * Roxanne Garland, DOE * Ali Jalalzadeh-Azar, NREL * Mike Seibert, NREL * Maria Ghirardi, NREL * Pin-Ching Maness, NREL * Tasio Melis, UC Berkeley * Gerald C. Dismukes - Princeton University * Bruce Logan, Penn State * DTI Team * Brian James * George Baum * Julie Perez * Kevin Baum Overview of 2009 Directed Technologies Inc. (DTI) Analysis 2 This presentation does not contain any proprietary, confidential, or otherwise restricted information  Start Date: April 2008

474

Solar Thermochemical Hydrogen Production Research (STCH): Thermochemical Cycle Selection and Investment Priority  

NLE Websites -- All DOE Office Websites (Extended Search)

1-3622 1-3622 Unlimited Release Printed May 2011 Solar Thermochemical Hydrogen Production Research (STCH) Thermochemical Cycle Selection and Investment Priority Robert Perret Prepared by Sandia National Laboratories Albuquerque, New Mexico 87185 and Livermore, California 94550 Sandia National Laboratories is a multi-program laboratory managed and operated by Sandia Corporation, a wholly owned subsidiary of Lockheed Martin Corporation, for the U.S. Department of Energy's National Nuclear Security Administration under contract DE-AC04-94AL85000. Approved for public release; further dissemination unlimited. 2 Issued by Sandia National Laboratories, operated for the United States Department of Energy by Sandia Corporation. NOTICE: This report was prepared as an account of work sponsored by an agency of the

475

Interactions of relativistic neon to nickel projectiles in hydrogen, elemental production cross sections  

Science Journals Connector (OSTI)

This paper reports the elemental production cross sections for 17 projectile-energy combinations with energies between 338 and 894 MeV/nucleon interacting in a liquid hydrogen target. These results were obtained from two runs at the LBL Bevalac using projectiles ranging from Ne22 to Ni58. Cross sections were measured for all fragment elements with charges greater than or equal to half the charge of the projectile. The results show that, over the energy and ion range investigated, the general decrease in cross section with decreasing fragment charge is strongly modified by the isospin of the projectile ion. Significant additional modifications of the cross sections due to the internal structure of the nucleus have also been seen. These include both pairing and shell effects. Differences in the cross sections due to the differing energies of the projectile are also considerable. 1996 The American Physical Society.

C. N. Knott et al.

1996-01-01T23:59:59.000Z

476

Analysis of the energy efficiency of solar aided biomass gasification for pure hydrogen production  

Science Journals Connector (OSTI)

Abstract This paper presents a simulative analysis of the energy efficiency of solar aided biomass gasification for pure hydrogen production. Solar heat has been considered as available at 250C in three gasification processes: i) gasification reactor followed by two water gas shift reactors and a pressure swing adsorber; ii) gasification reactor followed by an integrated membrane water gas shift reactor; iii) supercritical gasification reactor followed by two flash separators and a pressure swing adsorber. Simulations are performed with the commercial software Aspen Plus by considering biomass moisture content and the amount of solar heat as system variables. Results are presented in terms of energy and exergy system efficiency and are discussed and compared with the case of no solar integration.

Lucia Salemme; Marino Simeone; Riccardo Chirone; Piero Salatino

2014-01-01T23:59:59.000Z

477

Parametric Evaluation of Large-Scale High-Temperature Electrolysis Hydrogen Production Using Different Advanced Nuclear Reactor Heat Sources  

SciTech Connect

High Temperature Electrolysis (HTE), when coupled to an advanced nuclear reactor capable of operating at reactor outlet temperatures of 800 C to 950 C, has the potential to efficiently produce the large quantities of hydrogen needed to meet future energy and transportation needs. To evaluate the potential benefits of nuclear-driven hydrogen production, the UniSim process analysis software was used to evaluate different reactor concepts coupled to a reference HTE process design concept. The reference HTE concept included an Intermediate Heat Exchanger and intermediate helium loop to separate the reactor primary system from the HTE process loops and additional heat exchangers to transfer reactor heat from the intermediate loop to the HTE process loops. The two process loops consisted of the water/steam loop feeding the cathode side of a HTE electrolysis stack, and the sweep gas loop used to remove oxygen from the anode side. The UniSim model of the process loops included pumps to circulate the working fluids and heat exchangers to recover heat from the oxygen and hydrogen product streams to improve the overall hydrogen production efficiencies. The reference HTE process loop model was coupled to separate UniSim models developed for three different advanced reactor concepts (a high-temperature helium cooled reactor concept and two different supercritical CO2 reactor concepts). Sensitivity studies were then performed to evaluate the affect of reactor outlet temperature on the power cycle efficiency and overall hydrogen production efficiency for each of the reactor power cycles. The results of these sensitivity studies showed that overall power cycle and hydrogen production efficiencies increased with reactor outlet temperature, but the power cycles producing the highest efficiencies varied depending on the temperature range considered.

Edwin A. Harvego; Michael G. McKellar; James E. O'Brien; J. Stephen Herring

2009-09-01T23:59:59.000Z

478

Creation Of New Composite Materials For Hydrogen Energy Purposes. I. New Lines Of Membrane Production Technology  

Science Journals Connector (OSTI)

One of the main problems of hydrogen energy is separation and purification of hydrogen produced by various conversion methods from raw hydrocarbons. Carbon membranes can become ... and polymeric ones and enlarge ...

O. K. Alexeeva; M. M. Chelyak; A. A. Kotenko

2008-01-01T23:59:59.000Z

479

Infrastructure Costs Associated with Central Hydrogen Production from Biomass and Coal - DOE Hydrogen and Fuel Cells Program FY 2012 Annual Progress Report  

NLE Websites -- All DOE Office Websites (Extended Search)

7 7 FY 2012 Annual Progress Report DOE Hydrogen and Fuel Cells Program Darlene Steward (Primary Contact), Billy Roberts, Karen Webster National Renewable Energy Laboratory (NREL) 15013 Denver West Parkway Golden, CO 80401-3305 Phone: (303) 275-3837 Email: Darlene.Steward@nrel.gov DOE Manager HQ: Fred Joseck Phone: (202) 586-7932 Email: Fred.Joseck@hq.doe.gov Project Start Date: Fiscal Year (FY) 2010 Project End Date: Project continuation and direction determined annually by DOE FY 2012 Objectives Elucidate the location-dependent variability of * infrastructure costs for biomass- and coal-based central hydrogen production and delivery and the tradeoffs inherent in plant-location choices Provide modeling output and correlations for use in other * integrated analyses and tools

480

Maximum Hydrogen Production by Autothermal Steam Reforming of Bio-oil With NiCuZnAl Catalyst  

Science Journals Connector (OSTI)

Autothermal steam reforming (ATR) of bio-oil, which couples the endothermic steam reforming reaction with the exothermic partial oxidation, offers many advantages from a technical and economic point of view. Effective production of hydrogen through ATR of bio-oil was performed at lower temperature with NiCuZnAl catalyst. The highest hydrogen yield from bio-oil reached 64.3% with a nearly complete bio-oil conversion at 600 C, the ratio of steam to carbon fed (S/C) of 3 and the oxygen to carbon ratio (O/C) of 0.34. The reaction conditions in ATR including temperature, O/C, S/C and weight hourly space velocity can be used to control both hydrogen yield and products distribution. The comparison between the ATR and common steam reforming of bio-oil was studied. The mechanism of the ATR of bio-oil was also discussed.

Shi-zhi Yan; Qi Zhai; Quan-xin Li

2012-01-01T23:59:59.000Z

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481

Modified fuzzy algorithm based safety analysis of nuclear energy for sustainable hydrogen production in climate change prevention  

Science Journals Connector (OSTI)

Abstract The high temperature coolant of nuclear power plants (NPPs) has been investigated for the hydrogen production, which could be a major role of a green energy promotion. An accident of the high temperature gas cooled reactor (HTGR) is modeled for the stabilized hydrogen production using nuclear energy. For the clean energy resource pursuit in preventing the climate change, the hydrogen is one of very attractive energy sources. The non-operational data could be produced by the fuzzy set theory which is one of non-linear complex algorithms. So, the result can show the possibility of the event happening instead of the exact solutions. The random numbers are generated for membership numbers of the fuzzy function. The event manipulation is done by new membership numbers for the propagations. The final result is 1.0 in 8 times during 100months. So, the frequency is 0.08, or 8% of successful long-term cooling by conduction.

Tae Ho Woo

2014-01-01T23:59:59.000Z

482

Carbon Molecular Sieve Membrane as a True One Box Unit for Large Scale Hydrogen Production  

SciTech Connect

IGCC coal-fired power plants show promise for environmentally-benign power generation. In these plants coal is gasified to syngas then processed in a water gas-shift (WGS) reactor to maximize the hydrogen/CO{sub 2} content. The gas stream can then be separated into a hydrogen rich stream for power generation and/or further purified for sale as a chemical and a CO{sub 2} rich stream for the purpose of carbon capture and storage (CCS). Today, the separation is accomplished using conventional absorption/desorption processes with post CO{sub 2} compression. However, significant process complexity and energy penalties accrue with this approach, accounting for ~20% of the capital cost and ~27% parasitic energy consumption. Ideally, a ??one-box? process is preferred in which the syngas is fed directly to the WGS reactor without gas pre-treatment, converting the CO to hydrogen in the presence of H{sub 2}S and other impurities and delivering a clean hydrogen product for power generation or other uses. The development of such a process is the primary goal of this project. Our proposed "one-box" process includes a catalytic membrane reactor (MR) that makes use of a hydrogen-selective, carbon molecular sieve (CMS) membrane, and a sulfur-tolerant Co/Mo/Al{sub 2}O{sub 3} catalyst. The membrane reactor??s behavior has been investigated with a bench top unit for different experimental conditions and compared with the modeling results. The model is used to further investigate the design features of the proposed process. CO conversion >99% and hydrogen recovery >90% are feasible under the operating pressures available from IGCC. More importantly, the CMS membrane has demonstrated excellent selectivity for hydrogen over H{sub 2}S (>100), and shown no flux loss in the presence of a synthetic "tar"-like material, i.e., naphthalene. In summary, the proposed "one-box" process has been successfully demonstrated with the bench-top reactor. In parallel we have successfully designed and fabricated a full-scale CMS membrane and module for the proposed application. This full-scale membrane element is a 3" diameter with 30"L, composed of ~85 single CMS membrane tubes. The membrane tubes and bundles have demonstrated satisfactory thermal, hydrothermal, thermal cycling and chemical stabilities under an environment simulating the temperature, pressure and contaminant levels encountered in our proposed process. More importantly, the membrane module packed with the CMS bundle was tested for over 30 pressure cycles between ambient pressure and >300 -600 psi at 200 to 300°C without mechanical degradation. Finally, internal baffles have been designed and installed to improve flow distribution within the module, which delivered ?90% separation efficiency in comparison with the efficiency achieved with single membrane tubes. In summary, the full-scale CMS membrane element and module have been successfully developed and tested satisfactorily for our proposed one-box application; a test quantity of elements/modules have been fabricated for field testing. Multiple field tests have been performed under this project at National Carbon Capture Center (NCCC). The separation efficiency and performance stability of our full-scale membrane elements have been verified in testing conducted for times ranging from 100 to >250 hours of continuous exposure to coal/biomass gasifier off-gas for hydrogen enrichment with no gas pre-treatment for contaminants removal. In particular, "tar-like" contaminants were effectively rejected by the membrane with no evidence of fouling. In addition, testing was conducted using a hybrid membrane system, i.e., the CMS membrane in conjunction with the palladium membrane, to demonstrate that 99+% H{sub 2} purity and a high degree of CO{sub 2} capture could be achieved. In summary, the stability and performance of the full-scale hydrogen selective CMS membrane/module has been verified in multiple field tests in the presence of coal/biomass gasifier off-gas under this project. A promi

Paul Liu

2012-05-01T23:59:59.000Z

483

Feasibility Study of Hydrogen Production from Existing Nuclear Power Plants Using Alkaline Electrolysis  

SciTech Connect

The mid-range industrial market currently consumes 4.2 million metric tons of hydrogen per year and has an annual growth rate of 15% industries in this range require between 100 and 1000 kilograms of hydrogen per day and comprise a wide range of operations such as food hydrogenation, electronic chip fabrication, metals processing and nuclear reactor chemistry modulation.

Dana R. Swalla

2008-12-31T23:59:59.000Z

484

Coupling of Solar Energy to Hydrogen Peroxide Production in the Cyanobacterium Anacystis nidulans  

Science Journals Connector (OSTI)

...bioconversion of solar energy. Our experimental...strongly influence the capacity for hydrogen peroxide...bioconversion of solar energy. Our experimental...strongly influence the capacity for hydrogen peroxide...bioconversion of solar energy. Our experimental...strongly influence the capacity for hydrogen peroxide...

Mercedes Roncel; Jos A. Navarro; Miguel A. De la Rosa

1989-02-01T23:59:59.000Z

485

Redirecting Reductant Flux into Hydrogen Production via Metabolic Engineering of Fermentative Carbon Metabolism in a Cyanobacterium  

Science Journals Connector (OSTI)

...observed to evolve hydrogen in the dark at maximum rates approaching...activity. Int. J. Hydrogen Energy 33: 2014-2022. 4 Carrieri...by biological processes: a survey of literature. Int. J. Hydrogen Energy 26: 13-28. 9 Datta, R...

Kelsey McNeely; Yu Xu; Nick Bennette; Donald A. Bryant; G. Charles Dismukes

2010-06-11T23:59:59.000Z

486

The Bumpy Road to Hydrogen  

E-Print Network (OSTI)

in the cost of hydrogen production, distribution, and use.accelerate R&D of zero-emission hydrogen production methods.Renewable hydrogen production is a key area for focused

Sperling, Dan; Ogden, Joan M

2006-01-01T23:59:59.000Z

487

Hydrogen & Our Energy Future  

NLE Websites -- All DOE Office Websites (Extended Search)

Hydrogen Program Hydrogen Program www.hydrogen.energy.gov Hydrogen & Our Energy Future  | HydrOgEn & Our EnErgy FuturE U.S. Department of Energy Hydrogen Program www.hydrogen.energy.gov u.S. department of Energy |  www.hydrogen.energy.gov Hydrogen & Our Energy Future Contents Introduction ................................................... p.1 Hydrogen - An Overview ................................... p.3 Production ..................................................... p.5 Delivery ....................................................... p.15 Storage ........................................................ p.19 Application and Use ........................................ p.25 Safety, Codes and Standards ............................... p.33

488

Understanding Hydrogen in Bayer Process Emissions. 2. Hydrogen Production during the Degradation of Unsaturated Carboxylic Acids in Sodium Hydroxide Solutions  

Science Journals Connector (OSTI)

Allan Costine *, Joanne S.C. Loh , and Greg Power ... The stoichiometries of the formation of hydrogen and LMW carboxylates from the unsaturated carboxylates observed here are consistent with the regioselective hydration of the C?C double bond to form the corresponding ?-hydroxycarboxylates, which then undergo further degradation by an ionic mechanism involving base-catalyzed oxidation by water. ... Conditions: temperature = 250 C, time at temperature = 15 min, [NaOH] = 3.77 M. Legend: Ox = oxalate; For = formate; Ace = acetate; Lac = lactate; But = butanoate; Mal = malonate; Car = carbonate. ...

Allan Costine; Joanne S.C. Loh; Greg Power

2011-10-01T23:59:59.000Z

489

Optimization of Metabolic Capacity and Flux through Environmental Cues To Maximize Hydrogen Production by the Cyanobacterium Arthrospira (Spirulina) maxima  

Science Journals Connector (OSTI)

...that grow to high cell densities at high...from 2.8 to 9.4 solar-to-biomass energy...Zarrouks medium under solar irradiation (27...candidate to serve as a cell factory for large-scale hydrogen production because (i) Arthrospira...low-molecular-weight organic acids autofermentatively...

Gennady Ananyev; Damian Carrieri; G. Charles Dismukes

2008-08-01T23:59:59.000Z

490

Hydrogen production from inexhaustible supplies of fresh and salt water using microbial reverse-electrodialysis electrolysis cells  

Science Journals Connector (OSTI)

...renewable source of energy, such as solar (5), wind, or waste organic...collection for MREC operation. The pump and effluent reservoirs...9] where {delta}H is the heat of combustion (J/mol...BE ( 2005 ) Electrochemically assisted microbial production of hydrogen...

Younggy Kim; Bruce E. Logan

2011-01-01T23:59:59.000Z

491

Comment on Electron Source in Photoinduced Hydrogen Production on Pt-Supported TiO2 Particles  

Science Journals Connector (OSTI)

Comment on Electron Source in Photoinduced Hydrogen Production on Pt-Supported TiO2 Particles ... We can suggest at least three more likely (than Ti4+) sources for their mysterious electron donor:? (1) an overlooked inorganic species, (2) Ti3+, and/or (3) organic impurities. ...

Craig L. Perkins; Michael A. Henderson; David E. McCready; Greg S. Herman

2000-12-05T23:59:59.000Z