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      CO2/H2 원천분리 SMART 시스템의 수소생산특성 = Hydrogen Generation Characteristics of SMART System with Inherent CO2/H2 Separation

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      https://www.riss.kr/link?id=A104392936

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      다국어 초록 (Multilingual Abstract)

      To check the feasibility of SMART(Steam Methane Advanced Reforming Technology) system, an experimental investigation was performed. A fluidized bed reactor of diameter 0.052m was operated cyclically up to 10th cycle, alternating between reforming and regeneration conditions. FCR-4 catalyst was used as the reforming catalyst and calcined limestone(domestic, from Danyang) was used as the CO2 absorbent. Hydrogen concentration of 98.2% on a dry basis was reached at 650℃ for the first cycle. This value is much higher than H2 concentration of 73.6% in the reformer of conventional SMR (steam methane reforming) condition. The hydrogen concentration decreased because the CO2 capture capacity decreased as the number of cycles increased. However, the average hydrogen concentration at 10th cycle was 82.5% and this value is also higher than that of SMR. Based on these results, we could conclude that the SMART system can replace SMR system to generate pure hydrogen without HTS (high tempeature shift), LTS (low temperature shift) and CO2 separation process.
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      To check the feasibility of SMART(Steam Methane Advanced Reforming Technology) system, an experimental investigation was performed. A fluidized bed reactor of diameter 0.052m was operated cyclically up to 10th cycle, alternating between reforming and ...

      To check the feasibility of SMART(Steam Methane Advanced Reforming Technology) system, an experimental investigation was performed. A fluidized bed reactor of diameter 0.052m was operated cyclically up to 10th cycle, alternating between reforming and regeneration conditions. FCR-4 catalyst was used as the reforming catalyst and calcined limestone(domestic, from Danyang) was used as the CO2 absorbent. Hydrogen concentration of 98.2% on a dry basis was reached at 650℃ for the first cycle. This value is much higher than H2 concentration of 73.6% in the reformer of conventional SMR (steam methane reforming) condition. The hydrogen concentration decreased because the CO2 capture capacity decreased as the number of cycles increased. However, the average hydrogen concentration at 10th cycle was 82.5% and this value is also higher than that of SMR. Based on these results, we could conclude that the SMART system can replace SMR system to generate pure hydrogen without HTS (high tempeature shift), LTS (low temperature shift) and CO2 separation process.

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      참고문헌 (Reference)

      1 "Status for the Technology of Hydrogen Production from Natural Gas" 43 (43): 344-351, 2005

      2 "Sorption-enhanced Steam Reforming of Methane in a Fluidized Bed Reactor with Dolomite as CO2-acceptor" 61 : 1195-1202, 2006

      3 "Simultaneous CO2/SO2 Capture Characteristics of Three Limestones in a Fluidized Bed Reactor" 20 : 1621-1628, 2006

      4 "R&D Trends and Unit Process of Hydrogen Station" 43 (43): 331-343, 2005

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

      6 "Process Design and Selection of Operating Conditions for SMART System" 18 (18): 1-11, 2007

      7 "Performance Estimation and Process Selection for Chemical-Looping Hydrogen Generation System" 16 (16): 209-218, 2005

      8 "Enhancement of CaO for CO2 Capture in an FBC Environment" 96 : 187-195, 2003

      1 "Status for the Technology of Hydrogen Production from Natural Gas" 43 (43): 344-351, 2005

      2 "Sorption-enhanced Steam Reforming of Methane in a Fluidized Bed Reactor with Dolomite as CO2-acceptor" 61 : 1195-1202, 2006

      3 "Simultaneous CO2/SO2 Capture Characteristics of Three Limestones in a Fluidized Bed Reactor" 20 : 1621-1628, 2006

      4 "R&D Trends and Unit Process of Hydrogen Station" 43 (43): 331-343, 2005

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

      6 "Process Design and Selection of Operating Conditions for SMART System" 18 (18): 1-11, 2007

      7 "Performance Estimation and Process Selection for Chemical-Looping Hydrogen Generation System" 16 (16): 209-218, 2005

      8 "Enhancement of CaO for CO2 Capture in an FBC Environment" 96 : 187-195, 2003

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      학술지 이력

      학술지 이력
      연월일 이력구분 이력상세 등재구분
      2027 평가예정 재인증평가 신청대상 (재인증)
      2021-01-01 평가 등재학술지 유지 (재인증) KCI등재
      2018-08-16 학술지명변경 외국어명 : 미등록 -> Transactions of the Korean Hydrogen and New Energy Society KCI등재
      2018-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2015-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2011-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2009-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2006-01-01 평가 등재학술지 선정 (등재후보2차) KCI등재
      2005-05-30 학술지등록 한글명 : 한국수소및신에너지학회논문집
      외국어명 : 미등록
      KCI등재후보
      2005-01-01 평가 등재후보 1차 PASS (등재후보1차) KCI등재후보
      2003-07-01 평가 등재후보학술지 선정 (신규평가) KCI등재후보
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      학술지 인용정보

      학술지 인용정보
      기준연도 WOS-KCI 통합IF(2년) KCIF(2년) KCIF(3년)
      2016 0.25 0.25 0.22
      KCIF(4년) KCIF(5년) 중심성지수(3년) 즉시성지수
      0.25 0.23 0.371 0.17
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