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      SCOPUS KCI등재

      코크 생성 억제를 위한 이산화탄소 건식 개질 반응기의 최적 설계 = Optimal Design of Carbon Dioxide Dry Reformer for Suppressing Coke Formation

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      https://www.riss.kr/link?id=A105386706

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      다국어 초록 (Multilingual Abstract)

      As global warming accelerates, greenhouse gas reduction becomes more important. Carbon dioxide dry reforming is a promising green-house gas reduction technology that can obtain CO and H<sub>2</sub> which are high value-added materials by u...

      As global warming accelerates, greenhouse gas reduction becomes more important. Carbon dioxide dry reforming is a promising green-house gas reduction technology that can obtain CO and H<sub>2</sub> which are high value-added materials by utilizing CO<sub>2</sub> and CH<sub>4</sub> which are greenhouse gases. However, there is a significant coking problem during operation of the dry reforming reactor. Because the carbon dioxide dry reforming is a strong endothermic reaction, the temperature of the reactor drops near the reactor inlet and causes coke formation. To solve this problem, it is important to ensure that the reaction takes place in a temperature range where coke production is minimized. In this study, we proposed a design method that can maintain reaction temperature in the region where the coke is rarely generated by using the new catalyst configuration method. The design method also optimizes the reactor by solving the optimization problem which minimizes the reactor length for a given reaction conversion by using the fuel flow rate, catalyst density, and output temperature by section as optimization variables.

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      참고문헌 (Reference)

      1 김정묵, "메탄의 건식 개질을 이용한 이산화탄소의 재활용" 한국화학공학회 47 (47): 267-274, 2009

      2 Markewitz, P., "Worldwide Innovations in the Development of Carbon Capture Technologies and the Utilization of $CO_2$" 5 (5): 7281-7305, 2012

      3 Nikoo, M. K., "Thermodynamic Analysis of Carbon Dioxide Reforming of Methane in view of Solid Carbon Formation" 92 (92): 678-691, 2011

      4 Gadalla, A. M., "The Role of Catalyst Support on the Activity of Nickel for Reforming Methane with $CO_2$" 43 (43): 3049-3062, 1988

      5 Edwards, J. H., "The Chemistry of Methane Reforming with Carbon Dioxide and Its Current and Potential Applications" 42 (42): 269-289, 1995

      6 Benguerba, Y., "Modelling of Methane Dry Reforming over $Ni/Al_2O_3$ Catalyst in a Fixed-bed Catalytic Reactor" 114 (114): 109-119, 2015

      7 Lee, S., "Improved Configuration of Supported Nickel Catalysts in a Steam Reformer for Effective Hydrogen Production from Methane" 180 (180): 506-515, 2008

      8 Hwang, S., "Heterogeneous Catalytic Reactor Design with Optimum Temperature Profile I: Application of Catalyst Dilution and Side-stream Distribution" 59 (59): 4229- 4243, 2004

      9 Luyben, W. L., "Design and Control of the Dry Methane Reforming Process" 53 : 14423-14439, 2014

      10 Chubb, T. A., "Characteristics of $CO_2-CH_4$ Reforming Methanation Cycle Relevant to the Solchem ThermoChemical Power System" 24 (24): 341-345, 1980

      1 김정묵, "메탄의 건식 개질을 이용한 이산화탄소의 재활용" 한국화학공학회 47 (47): 267-274, 2009

      2 Markewitz, P., "Worldwide Innovations in the Development of Carbon Capture Technologies and the Utilization of $CO_2$" 5 (5): 7281-7305, 2012

      3 Nikoo, M. K., "Thermodynamic Analysis of Carbon Dioxide Reforming of Methane in view of Solid Carbon Formation" 92 (92): 678-691, 2011

      4 Gadalla, A. M., "The Role of Catalyst Support on the Activity of Nickel for Reforming Methane with $CO_2$" 43 (43): 3049-3062, 1988

      5 Edwards, J. H., "The Chemistry of Methane Reforming with Carbon Dioxide and Its Current and Potential Applications" 42 (42): 269-289, 1995

      6 Benguerba, Y., "Modelling of Methane Dry Reforming over $Ni/Al_2O_3$ Catalyst in a Fixed-bed Catalytic Reactor" 114 (114): 109-119, 2015

      7 Lee, S., "Improved Configuration of Supported Nickel Catalysts in a Steam Reformer for Effective Hydrogen Production from Methane" 180 (180): 506-515, 2008

      8 Hwang, S., "Heterogeneous Catalytic Reactor Design with Optimum Temperature Profile I: Application of Catalyst Dilution and Side-stream Distribution" 59 (59): 4229- 4243, 2004

      9 Luyben, W. L., "Design and Control of the Dry Methane Reforming Process" 53 : 14423-14439, 2014

      10 Chubb, T. A., "Characteristics of $CO_2-CH_4$ Reforming Methanation Cycle Relevant to the Solchem ThermoChemical Power System" 24 (24): 341-345, 1980

      11 Luyben, W. L., "Catalyst Dilution to Improve Dynamic Controllability of Cooled Tubular Reactors" 37 : 184-190, 2012

      12 Richardson, J. T., "Carbon Dioxide Reforming of Methane with Supported Rhodium" 61 (61): 293-309, 1990

      13 Wang, S., "Carbon Dioxide Reforming of Methane to Produce Synthesis Gas over Metal-supported Catalysts: State of the Art" 10 (10): 896-904, 1996

      14 Moon, K.-I., "Carbon Dioxide Reforming of Methane over Nickel based Catalyst, Department of Chemical Engineering" 111-, 1996

      15 Mun, G. I., "Carbon Dioxide Reforming of Methane over Nickel Based Catalysts I. Comparison with Steam Reforming" 35 (35): 883-883, 1997

      16 Pakhare, D., "A Review of Dry ($CO_2$) Reforming of Methane over Noble Metal Catalysts" 43 (43): 7813-7837, 2014

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      학술지 이력

      학술지 이력
      연월일 이력구분 이력상세 등재구분
      2023 평가예정 해외DB학술지평가 신청대상 (해외등재 학술지 평가)
      2020-01-01 평가 등재학술지 유지 (해외등재 학술지 평가) KCI등재
      2013-01-01 평가 등재 1차 FAIL (등재유지) KCI등재
      2010-12-02 학술지명변경 한글명 : 화학공학 -> Korean Chemical Engineering Research(HWAHAK KONGHAK) KCI등재
      2010-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2009-08-25 학술지명변경 외국어명 : Korean Chem. Eng. Res. -> Korean Chemical Engineering Research KCI등재
      2008-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2007-09-27 학회명변경 영문명 : The Korean Institute Of Chemical Engineers -> The Korean Institute of Chemical Engineers KCI등재
      2006-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2004-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2001-07-01 평가 등재학술지 선정 (등재후보2차) KCI등재
      1999-01-01 평가 등재후보학술지 선정 (신규평가) KCI등재후보
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      학술지 인용정보

      학술지 인용정보
      기준연도 WOS-KCI 통합IF(2년) KCIF(2년) KCIF(3년)
      2016 0.43 0.43 0.4
      KCIF(4년) KCIF(5년) 중심성지수(3년) 즉시성지수
      0.37 0.35 0.496 0.11
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