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      3D-IR Matrix 버너 개질기를 활용한 모사 바이오가스 수증기 개질 연구 = The Study of Steam Reforming for Model Bioigas using 3D-IR Matrix Burner Reformer

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      https://www.riss.kr/link?id=A103868571

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      다국어 초록 (Multilingual Abstract) kakao i 다국어 번역

      The use of biogas as an energy source reduces the chance of possible emission of two greenhouse gases, CH_4 and CO_2, into the atmosphere at the same time. Its nature of being a reproducible energy source makes its use even more attractive. This research if for the hydrogen production through the steam reforming of the biogas. The biogas utilized 3D-IR matrix burner in which the surface combustion is applied. The nickel catalyst was used inside a reformer. Parametric screening studies were achieved as Steam/Carbon ratio, biogas component ratio, Space velocity and Reformer temperature. When the condition of Steam/Carbon ratio,CH_4/CO_2 ratio, Space velocity and Refomer temperature were 3.25, 60%:40%, 19.32L/g・hr and 700℃respectively, the hydrogen concentration and methane conversion rate were showed maximum values. Under the condition mentioned above, H_2 concentration was 73.9% and methane conversion rate was 98.9%.
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      The use of biogas as an energy source reduces the chance of possible emission of two greenhouse gases, CH_4 and CO_2, into the atmosphere at the same time. Its nature of being a reproducible energy source makes its use even more attractive. This resea...

      The use of biogas as an energy source reduces the chance of possible emission of two greenhouse gases, CH_4 and CO_2, into the atmosphere at the same time. Its nature of being a reproducible energy source makes its use even more attractive. This research if for the hydrogen production through the steam reforming of the biogas. The biogas utilized 3D-IR matrix burner in which the surface combustion is applied. The nickel catalyst was used inside a reformer. Parametric screening studies were achieved as Steam/Carbon ratio, biogas component ratio, Space velocity and Reformer temperature. When the condition of Steam/Carbon ratio,CH_4/CO_2 ratio, Space velocity and Refomer temperature were 3.25, 60%:40%, 19.32L/g・hr and 700℃respectively, the hydrogen concentration and methane conversion rate were showed maximum values. Under the condition mentioned above, H_2 concentration was 73.9% and methane conversion rate was 98.9%.

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      참고문헌 (Reference)

      1 A. E. Lutz, "Thermodynamic analysis of hydrogen production by partial oxidation reforming" 29 : 809-816, 2004

      2 A. I. Bakry, "Stabilized Premixed Combustion within Atmospheric Gas Porous Inert Medium (PIM) Burner" 1-9, 2006

      3 Y. N. Chun, "Hydrogen generation from biogas reforming using a gliding arc plasma-catalyst reformer" 148 : 283-289, 2009

      4 G. Kolios, "Heatintegrated reactor concepts for catalytic refoming and automotive exhaust purification" 70 : 16-30, 2007

      5 M. Ashrafi, "Experimental study of model biogas catalytic steam reforming: 1. Thermodynamic optimization" 22 : 4182-4189, 2008

      6 P. Beckhaus, "Dynamic of H2 production by steam reforming" 127 : 294-299, 2004

      7 P. Kolbitsch, "Catalytic steam reforming of model biogas" 87 : 701-706, 2008

      8 D. G. Avraam, "An experimental and theoretical approach for the biogas steam reforming reaction" 35 : 9818-9827, 2010

      9 T. Takeno, "An excess enthalpy flame theory" 20 : 73-84, 1979

      10 S. G. Wang, "A detailed mechanism of thermal CO2 reforming of CH4" 673 : 181-189, 2004

      1 A. E. Lutz, "Thermodynamic analysis of hydrogen production by partial oxidation reforming" 29 : 809-816, 2004

      2 A. I. Bakry, "Stabilized Premixed Combustion within Atmospheric Gas Porous Inert Medium (PIM) Burner" 1-9, 2006

      3 Y. N. Chun, "Hydrogen generation from biogas reforming using a gliding arc plasma-catalyst reformer" 148 : 283-289, 2009

      4 G. Kolios, "Heatintegrated reactor concepts for catalytic refoming and automotive exhaust purification" 70 : 16-30, 2007

      5 M. Ashrafi, "Experimental study of model biogas catalytic steam reforming: 1. Thermodynamic optimization" 22 : 4182-4189, 2008

      6 P. Beckhaus, "Dynamic of H2 production by steam reforming" 127 : 294-299, 2004

      7 P. Kolbitsch, "Catalytic steam reforming of model biogas" 87 : 701-706, 2008

      8 D. G. Avraam, "An experimental and theoretical approach for the biogas steam reforming reaction" 35 : 9818-9827, 2010

      9 T. Takeno, "An excess enthalpy flame theory" 20 : 73-84, 1979

      10 S. G. Wang, "A detailed mechanism of thermal CO2 reforming of CH4" 673 : 181-189, 2004

      11 G. Petitpas, "A comparative study of non-thermal plasma assisted reforming technologies" 32 (32): 2848-2867, 2007

      12 김성천, "3상 교류 부채꼴 방전을 이용한 메탄으로부터 수소 생산" 한국수소및신에너지학회 18 (18): 132-139, 2007

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      유사연구자 (20) 활용도상위20명

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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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