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    SEWGS 공정용 CO2 흡수제들의 흡수능력에 미치는 조업변수들의 영향 = Effects of Operating Variables on Sorption Capacity of CO2 Absorbents for SEWGS Process

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    https://www.riss.kr/link?id=A99537925

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    The Effects of operating variables on reactivity of two CO2 absorbents (PKM1-SU and P4-600) for SEWGS process were investigated in a pressurized fluidized bed reactor. For both CO2 absorbents, CO2 sorption capacity decreased as the number of absorption-regeneration cycles increased. PKM1-SU absorbent represented higher CO2 sorption capacity than that of P4-600 absorbent. However, P4-600 absorbent represented better performance than PKM1-SU absorbent from the view points of regeneration temperature and regeneration rate. For PKM1-SU absorbent, CO2 sorption capacity increased as the steam concentration increased. However, CO2 sorption capacity increased initially as the steam concentration increased from 5% to 10%, but maintained thereafter for P4-600 absorbent. For both CO2 absorbents, CO2 sorption capacity increased as the final regeneration temperature increased. For PKM1-SU absorbent, CO2 sorption capacity increased as the pressure increased and the increment tendency was drastic at higher pressure than 15bar.
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    The Effects of operating variables on reactivity of two CO2 absorbents (PKM1-SU and P4-600) for SEWGS process were investigated in a pressurized fluidized bed reactor. For both CO2 absorbents, CO2 sorption capacity decreased as the number of absorptio...

    The Effects of operating variables on reactivity of two CO2 absorbents (PKM1-SU and P4-600) for SEWGS process were investigated in a pressurized fluidized bed reactor. For both CO2 absorbents, CO2 sorption capacity decreased as the number of absorption-regeneration cycles increased. PKM1-SU absorbent represented higher CO2 sorption capacity than that of P4-600 absorbent. However, P4-600 absorbent represented better performance than PKM1-SU absorbent from the view points of regeneration temperature and regeneration rate. For PKM1-SU absorbent, CO2 sorption capacity increased as the steam concentration increased. However, CO2 sorption capacity increased initially as the steam concentration increased from 5% to 10%, but maintained thereafter for P4-600 absorbent. For both CO2 absorbents, CO2 sorption capacity increased as the final regeneration temperature increased. For PKM1-SU absorbent, CO2 sorption capacity increased as the pressure increased and the increment tendency was drastic at higher pressure than 15bar.

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    참고문헌 (Reference)

    1 류호정, "회수증진 수성가스화 시스템의 공정구성 및 조업조건 선정" 한국수소및신에너지학회 20 (20): 168-178, 2009

    2 류호정, "회분식 유동층 반응기에서 촉매함량 변화에 따른 WGS 촉매의 반응특성" 한국수소및신에너지학회 22 (22): 465-473, 2011

    3 Lee, J. B., "Study on Hybrid Materials of WGS Cataylst and CO2 Sorbent for SEWGS Process" 372-, 2010

    4 Eric, D., "Sour SEWGS Applicaion in IGCC" 2011

    5 Ryu, H. J., "Selection of WGS Catalyst and CO2 Absorbent for Pre-combustion CO2 Capture" 2011

    6 Ryu, H. J., "SEWGS Reaction with Mixture of WGS Catalyst and CO2 Absorbent in a Fluidized Bed Reactor" 230-, 2011

    7 IEA, "Prospects for Hydrogen and Fuel Cells" IEA Books 49-55, 2005

    8 Lee, J. M., "Enhancement of CO2 Sorption Uptake on Hydrotalcite by Impregnation with K2CO3" 26 (26): 18788-18797, 2010

    9 James, R., "Clean Coal technology Status: CO2 Capture and Storage"

    10 Beavis, R., "CACHET: Outline of Project Objectives and Base Case" IFP 2008

    1 류호정, "회수증진 수성가스화 시스템의 공정구성 및 조업조건 선정" 한국수소및신에너지학회 20 (20): 168-178, 2009

    2 류호정, "회분식 유동층 반응기에서 촉매함량 변화에 따른 WGS 촉매의 반응특성" 한국수소및신에너지학회 22 (22): 465-473, 2011

    3 Lee, J. B., "Study on Hybrid Materials of WGS Cataylst and CO2 Sorbent for SEWGS Process" 372-, 2010

    4 Eric, D., "Sour SEWGS Applicaion in IGCC" 2011

    5 Ryu, H. J., "Selection of WGS Catalyst and CO2 Absorbent for Pre-combustion CO2 Capture" 2011

    6 Ryu, H. J., "SEWGS Reaction with Mixture of WGS Catalyst and CO2 Absorbent in a Fluidized Bed Reactor" 230-, 2011

    7 IEA, "Prospects for Hydrogen and Fuel Cells" IEA Books 49-55, 2005

    8 Lee, J. M., "Enhancement of CO2 Sorption Uptake on Hydrotalcite by Impregnation with K2CO3" 26 (26): 18788-18797, 2010

    9 James, R., "Clean Coal technology Status: CO2 Capture and Storage"

    10 Beavis, R., "CACHET: Outline of Project Objectives and Base Case" IFP 2008

    11 Maurstad, O., "An Overview of Coal Based Integrated Gasification Combined Cycle (IGCC) Technology" 1-43, 2008

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    2006-01-01 등재 등재학술지 유지 (등재유지) KCI등재
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