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Sample records for akms aznm camx

  1. CAMX - A High Performance Cutting Technique for Underwater Use

    SciTech Connect (OSTI)

    Bach, Fr.-W.; Versemann, R.; Bienia, H.; Kremer, G.

    2003-02-27

    During the past years a new cutting technology, the CAMX-process-family (Contact-Arc-Metal-X [X is for Cutting, Grinding and Drilling]) was developed at the Institute of Materials Science in Hanover. These are electro-thermal underwater separation processes for metallic structures. The CAMX technology covers the Contact-Arc-Metal- Cutting (CAMC) with a sword-like cutting electrode, the Contact-Arc-Metal-Grinding (CAMG) with a rotating electrode and the Contact-Arc-Metal-Drilling (CAMD) with a wrap mechanism to fix and carry the workpiece. There are no limitations of CAMC concerning the capability of cutting complicated structures of workpieces. Undercuts and cavities in the workpiece do not affect the CAMC. The CAMG is a separation process for straight cuts with a very high cutting speed. The CAMD is a technology to drill holes or pocket holes of any geometry. With the integrated wrap mechanism it is possible to fix and carry workpieces, which are not to handle with conventional mechanisms.

  2. U.S. Energy Information Administration | Annual Energy Outlook...

    Annual Energy Outlook [U.S. Energy Information Administration (EIA)]

    OH 1. NE 3. S1 4. S2 5. GF 6. OH 7. EN AL,MS MN,ND,SD IA,NE,MO,KS TX,LA,OK,AR MT,WY,ID CO,UT,NV AZ,NM 9. AM 11. C2 12. WS 13. MT 14. CU 15. ZN WV,MD,DC,DE 2. YP...

  3. Microsoft Word - Document2

    Open Energy Info (EERE)

    min, average, and max average CO 2 emissions by month for AZNM subregion (lbs CO 2 MWh load) 800 1,100 1,400 1,700 January 800 1,100 1,400 1,700 February 800 1,100 1,400 1,700...

  4. MEMORANDUM

    Office of Legacy Management (LM)

    '%1mYLz%&E2 xy (on basis of records reviewed) q No Radioactive c Health Physics .Protectio" 6 Little or None F AKME D responsibi 1,i ty E Contractor'responsibility ...

  5. Evaluation of Wax Deposition and its Control during Production...

    Office of Scientific and Technical Information (OSTI)

    ... of the modified model to account for change in heat capacity during the ... A.K.M., J.Nighswander, and N.Joshi, "A Systematic Approach for Characterizing Hydrocarbon ...

  6. Sandia Participates in the Second Annual Composites and Advanced...

    Broader source: All U.S. Department of Energy (DOE) Office Webpages (Extended Search)

    ... Research on composite material applications in wind energy at the CAMX conference in Dallas, Texas, October 26-29, 2015. The papers detailed a novel composite process model ...

  7. AMO Weekly Announcements 11/5/15 | Department of Energy

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

    5/15 AMO Weekly Announcements 11/5/15 November 5, 2015 - 11:00am Addthis AMO Technology Manager Leads Education Discussion at CAMX Kelly Visconti, a technology manager with the Department of Energy's (DOE) Advanced Manufacturing Office, led an educational session at The Composites and Advanced Materials Expo (CAMX) last month in Dallas, TX. She spoke on the topic of "Lightweight Composites for Clean Energy." Read a recent article published by Composite Manufacturing Magazine on

  8. Annual Energy Outlook 2015 - Appendix F

    Gasoline and Diesel Fuel Update (EIA)

    8 Regional maps Figure F7. Coal demand regions Figure F7. Coal Demand Regions CT,MA,ME,NH,RI,VT OH 1. NE 3. S1 4. S2 5. GF 6. OH 7. EN AL,MS MN,ND,SD IA,NE,MO,KS TX,LA,OK,AR MT,WY,ID CO,UT,NV AZ,NM 9. AM 11. C2 12. WS 13. MT 14. CU 15. ZN WV,MD,DC,DE 2. YP Region Content Region Code NY,PA,NJ VA,NC,SC GA,FL IN,IL,MI,WI Region Content Region Code 14. CU 13. MT 16. PC 15. ZN 12. WS 11. C2 9. AM 5. GF 8. KT 4. S2 7. EN 6. OH 2. YP 1. NE 3. S1 10. C1 KY,TN 8. KT 16. PC AK,HI,WA,OR,CA 10. C1

  9. MPO SAN ANTONIO - BEXAR COUNTY METROPOLITAN PLANNING ORGANIZATION

    Energy Savers [EERE]

    5-11 Figure 5-11: 1-Hour Ozone Time Series Observed (C506) v. Predicted (CAMx) for WRF AACOG Base Case Run 3, 2006 5-12 5.3.2 Hourly NO X Time Series Time series plots of modeled and predicted hourly NO X for each monitor located in the San Antonio MSA were constructed. The model over predicted NO X emissions at the C58 monitor on almost every day during the June 2006 episode. The average predicted hourly NO X was 7.3 ppb, while the average observed hourly NO X was only 3.9 ppb. Likewise, the

  10. X Time Series

    Energy Savers [EERE]

    11 Figure 5-11: 1-Hour Ozone Time Series Observed (C506) v. Predicted (CAMx) for WRF AACOG Base Case Run 3, 2006 5-12 5.3.2 Hourly NO X Time Series Time series plots of modeled and predicted hourly NO X for each monitor located in the San Antonio MSA were constructed. The model over predicted NO X emissions at the C58 monitor on almost every day during the June 2006 episode. The average predicted hourly NO X was 7.3 ppb, while the average observed hourly NO X was only 3.9 ppb. Likewise, the

  11. Novel Flow Sheet for Low Energy CO2 Capture Enabled by Biocatalyst Delivery System

    SciTech Connect (OSTI)

    Reardon, John; Shaffer, Alex; Vaysman, Vladimir

    2015-02-01

    This report documents a preliminary Techno-Economic Assessment (TEA) for processes utilizing Akermin’s second generation biocatalyst delivery system to enhance AKM24, a non- volatile salt solution for CO2 capture. Biocatalyst enhanced AKM24 offers the potential to reduce the cost of CO2 capture in flue gas applications due to its improved equilibrium and stoichiometric properties that result in double the absorption capacity relative to previously demonstrated biocatalyst enhanced solvents. The study assumes a new supercritical pulverized coal fired power plant with a net output of 550 MWe after 90% CO2 capture and uses the June 2011 cost basis (August 2012 update of Bituminous Baseline Study, or BBS). Power plant modeling, capital cost review, and economic calculations were provided by WorleyParsons. Rate-based CO2 capture process modeling and equipment sizing was performed by Akermin using AspenPlus® V8.4, customized to accurately predict thermodynamics, kinetics, and physical properties of the AKM-24 solvent based on available laboratory data. Equipment capital costs were estimated using Aspen Process Economic Analyzer™ which compared well with published baseline cost estimates. Quotes of equipment costs and power consumption for vacuum blower and CO2 compression equipment were also provided by Man Diesel & Turbo. Three process scenarios were examined for Akermin biocatalyst enhanced solvent systems including: Case-1A: an absorption-desorption system operated with a reboiler pressure of 0.16 bara (60°C); Case-2A: an absorption-desorption system with moderate vacuum assisted regeneration at 0.40 bara (80°C); and finally, Case-2B: a conventional absorption-desorption system with near atmospheric pressure regeneration at 1.07 bara (105°C). The estimated increases in cost of electricity (ICOE) for these cases were $58.1/MWh, $47.3/MWh and $46.4/MWh, respectively. Case 2B had the best results for this analysis achieving an estimated 30% reduction in ICOE relative to the NETL Case 12 (v2) baseline of $66.3/MWh ICOE. Likewise, Case-2B achieved capture costs of $53.0/tCO2 and 65.7/tCO2 avoided, which equates to 20.2% and 31.4% savings relative to the Case 12 baseline ($66.4/tCO2 and $95.9/tCO2 avoided). While Case 2A and 2B have similar results, Case 2A requires further development. Focus on Case 2B is recommended for this project because its cost performance is closest to the DOE goals, and has it has the best potential to achieve a successful demonstration at the next scale.