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Title: A CYBER-PHYSICAL OBSERVER FOR FLUIDIZED BED CHEMICAL LOOPING PROCESS DEVELOPMENT

Authors:
 [1];  [1];  [1];  [2];  [3];  [1];  [1];  [4]
  1. National Energy Technology Lab. (NETL), Morgantown, WV (United States)
  2. NETL/AMES Laboratory
  3. NETL/REM
  4. Ames Lab., Ames, IA (United States)
Publication Date:
Research Org.:
National Energy Technology Lab. (NETL), Pittsburgh, PA, and Morgantown, WV (United States). In-house Research
Sponsoring Org.:
USDOE Office of Fossil Energy (FE)
OSTI Identifier:
1433644
Report Number(s):
NETL-PUB-20842
Resource Type:
Conference
Resource Relation:
Conference: 12th International Conference on Fluidized Bed Technology (CFB 12), Ed. W. Nowak, M. Sciazko, and P. Mirek, Krakow, Poland, May 23-25, 2017
Country of Publication:
United States
Language:
English

Citation Formats

Shadle, Lawrence J., Bayham, Samuel, Tucker, David, Pezzini, Paolo, Monazam, Esmail, Weber, Justin, Breault, Ronald, and Bryden, Mark. A CYBER-PHYSICAL OBSERVER FOR FLUIDIZED BED CHEMICAL LOOPING PROCESS DEVELOPMENT. United States: N. p., 2017. Web.
Shadle, Lawrence J., Bayham, Samuel, Tucker, David, Pezzini, Paolo, Monazam, Esmail, Weber, Justin, Breault, Ronald, & Bryden, Mark. A CYBER-PHYSICAL OBSERVER FOR FLUIDIZED BED CHEMICAL LOOPING PROCESS DEVELOPMENT. United States.
Shadle, Lawrence J., Bayham, Samuel, Tucker, David, Pezzini, Paolo, Monazam, Esmail, Weber, Justin, Breault, Ronald, and Bryden, Mark. Tue . "A CYBER-PHYSICAL OBSERVER FOR FLUIDIZED BED CHEMICAL LOOPING PROCESS DEVELOPMENT". United States. doi:. https://www.osti.gov/servlets/purl/1433644.
@article{osti_1433644,
title = {A CYBER-PHYSICAL OBSERVER FOR FLUIDIZED BED CHEMICAL LOOPING PROCESS DEVELOPMENT},
author = {Shadle, Lawrence J. and Bayham, Samuel and Tucker, David and Pezzini, Paolo and Monazam, Esmail and Weber, Justin and Breault, Ronald and Bryden, Mark},
abstractNote = {},
doi = {},
journal = {},
number = ,
volume = ,
place = {United States},
year = {Tue May 23 00:00:00 EDT 2017},
month = {Tue May 23 00:00:00 EDT 2017}
}

Conference:
Other availability
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  • Chemical Looping Combustion is a novel combustion technology for the inherent separation of the greenhouse gas, CO{sub 2}. In 1983, Richter and Knoche proposed reversible combustion, which utilized both the oxidation and reduction of metal. Metal associated with its oxidized form as an oxygen carrier was circulated between two reactors--oxidizer and reducer. In the reducer, the solid oxygen carrier reacts with the fuel to produce CO{sub 2}, H{sub 2}O and elemental metal only. Pure CO{sub 2} will be obtained in the exit gas stream from the reducer after H{sub 2}O is condensed. The pure CO{sub 2} is ready for subsequentmore » sequestration. In the oxidizer, the elemental metal reacts with air to form metal oxide and separate oxygen from nitrogen. Only nitrogen and some unused oxygen are emitted from the oxidizer. The advantage of CLC compared to normal combustion is that CO{sub 2} is not diluted with nitrogen but obtained in a relatively pure form without any energy needed for separation. In addition to the energy-free purification of CO{sub 2}, the CLC process also provides two other benefits. First, NO{sub x} formation can be largely eliminated. Secondly, the thermal efficiency of a CLC system is very high. Presently, the CLC process has only been used with natural gas. An oxygen carrier based on an energy balance analysis and thermodynamics analysis was selected. Copper (Cu) seems to be the best choice for the CLC system for solid fuels. From this project, the mechanisms of CuO reduction by solid fuels may be as follows: (1) If pyrolysis products of solid fuels are available, reduction of CuO could start at about 400 C or less. (2) If pyrolysis products of solid fuels are unavailable and the reduction temperature is lower, reduction of CuO could occur at an onset temperature of about 500 C, char gasification reactivity in CO{sub 2} was lower at lower temperatures. (3) If pyrolysis products of solid fuels are unavailable and the reduction temperature is higher than 750 C, all reaction reactivities were improved, especially the CO{sub 2} gasification reactivity of char. Thus, the reduction of CuO by the gasification product CO could proceed quickly. Based on the results obtained, the following coal characteristics would be desirable for the Chemical Looping Combustion process: high volatile matter with a high reactivity of the char produced. PRB coal meets these criteria while being comparatively less expensive and also very abundant. The high moisture content present in PRB coal might also increase the reactivity for char gasification through the development of pore structure and specific surface area in the char during pyrolysis. Biomass materials are also suitable, considering the reaction mechanism of CLC system of solid fuels. The feasibility of the chemical looping combustion process of solid fuels was verified by focusing on PRB coal and biomass. Based on PRB coal as the preferred solid fuel in the development of the CLC system, the mass, energy and system in a dual reactor recirculation system has been determined. In the Cu oxidation tests, it was confirmed that the heating rate is the most important effect on the Cu oxidation process. Lower heating rates and lower operational temperatures would result in incomplete conversion of Cu to CuO. Cu{sub 2}O may be the intermediate product. The operating temperature did not affect the reaction rate of the oxidation process. Under any operating conditions, the exothermic properties are clearly shown.« less
  • The coal to hydrogen project utilizes the iron/iron oxide looping process to produce high purity hydrogen. The input energy for the process is provided by syngas coming from gasification process of coal. The reaction pathways for this process have been studied and favorable conditions for energy efficient operation have been identified. The Magnetically Stabilized Porous Structure (MSPS) is invented. It is fabricated from iron and silica particles and its repeatable high performance has been demonstrated through many experiments under various conditions in thermogravimetric analyzer, a lab-scale reactor, and a large scale reactor. The chemical reaction kinetics for both oxidation andmore » reduction steps has been investigated thoroughly inside MSPS as well as on the surface of very smooth iron rod. Hydrogen, CO, and syngas have been tested individually as the reducing agent in reduction step and their performance is compared. Syngas is found to be the most pragmatic reducing agent for the two-step water splitting process. The transport properties of MSPS including porosity, permeability, and effective thermal conductivity are determined based on high resolution 3D CT x-ray images obtained at Argonne National Laboratory and pore-level simulations using a lattice Boltzmann Equation (LBE)-based mesoscopic model developed during this investigation. The results of those measurements and simulations provide necessary inputs to the development of a reliable volume-averaging-based continuum model that is used to simulate the dynamics of the redox process in MSPS. Extensive efforts have been devoted to simulate the redox process in MSPS by developing a continuum model consist of various modules for conductive and radiative heat transfer, fluid flow, species transport, and reaction kinetics. Both the Lagrangian and Eulerian approaches for species transport of chemically reacting flow in porous media have been investigated and verified numerically. Both approaches lead to correct prediction of hydrogen production rates over a large range of experimental conditions in the laboratory scale reactor and the bench-scale reactor. In the economic analysis, a comparison of the hydrogen production plants using iron/iron oxide looping cycle and the conventional process has been presented. Plant configurations are developed for the iron/iron oxide looping cycle. The study suggests a higher electric power generation but a lower hydrogen production efficiency comparing with the conventional process. Additionally, it was shown that the price of H{sub 2} obtained from our reactor can be as low as $1.7/kg, which is 22% lower than the current price of the H{sub 2} obtained from reforming plants.« less