1 kWe sodium borohydride hydrogen generation system Part II:: Reactor modeling
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作者:
Zhang, Jinsong
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Purdue Univ, Sch Mech Engn, Energy Ctr Discovery Pk, W Lafayette, IN 47907 USAPurdue Univ, Sch Mech Engn, Energy Ctr Discovery Pk, W Lafayette, IN 47907 USA
Zhang, Jinsong
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Zheng, Yuan
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Purdue Univ, Sch Mech Engn, Energy Ctr Discovery Pk, W Lafayette, IN 47907 USAPurdue Univ, Sch Mech Engn, Energy Ctr Discovery Pk, W Lafayette, IN 47907 USA
Zheng, Yuan
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Gore, Jay P.
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Purdue Univ, Sch Mech Engn, Energy Ctr Discovery Pk, W Lafayette, IN 47907 USAPurdue Univ, Sch Mech Engn, Energy Ctr Discovery Pk, W Lafayette, IN 47907 USA
Gore, Jay P.
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Mudawar, Issarn
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Purdue Univ, Sch Mech Engn, Energy Ctr Discovery Pk, W Lafayette, IN 47907 USAPurdue Univ, Sch Mech Engn, Energy Ctr Discovery Pk, W Lafayette, IN 47907 USA
Mudawar, Issarn
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Fisher, T. S.
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Purdue Univ, Sch Mech Engn, Energy Ctr Discovery Pk, W Lafayette, IN 47907 USAPurdue Univ, Sch Mech Engn, Energy Ctr Discovery Pk, W Lafayette, IN 47907 USA
Fisher, T. S.
[1
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[1] Purdue Univ, Sch Mech Engn, Energy Ctr Discovery Pk, W Lafayette, IN 47907 USA
Sodium borohydride (NaBH4) hydrogen storage systems offer many advantages for hydrogen storage applications. The physical processes inside a NaBH4 packed bed reactor involve multi-component and multi-phase flow and multi-mode heat and mass transfer. These processes are also coupled with reaction kinetics. To guide reactor design and optimization, a reactor model involving all of these processes is desired. A one-dimensional numerical model in conjunction with the assumption of homogeneous catalysis is developed in this study. Two submodels have been created to simulate non-isothermal water evaporation processes and pressure drop of two-phase flow through the porous medium. The diffusion coefficient of liquid inside the porous catalyst pellets and the mass transfer coefficient of water vapor are estimated by fitting experimental data at one specified condition and have been verified at other conditions. The predicted temperature profiles, fuel conversion, relative humidity and pressure drops match experimental data reasonably well. (C) 2007 Elsevier B.V. All rights reserved.
机构:
Penn State Univ, Clean Fuels & Catalysis Program, EMS Energy Inst, University Pk, PA 16802 USA
Penn State Univ, Dept Energy & Mineral Engn, University Pk, PA 16802 USAKorea Inst Ind Technol KITECH, Surface Technol Team, Inchon 406840, South Korea
Kim, Hyun Jae
Shin, Kyoung-Jin
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Korea Inst Ind Technol KITECH, Surface Technol Team, Inchon 406840, South KoreaKorea Inst Ind Technol KITECH, Surface Technol Team, Inchon 406840, South Korea
Shin, Kyoung-Jin
Kim, Hyun-Jong
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Korea Inst Ind Technol KITECH, Surface Technol Team, Inchon 406840, South KoreaKorea Inst Ind Technol KITECH, Surface Technol Team, Inchon 406840, South Korea
Kim, Hyun-Jong
Han, M. K.
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Korea Inst Ind Technol KITECH, Surface Technol Team, Inchon 406840, South KoreaKorea Inst Ind Technol KITECH, Surface Technol Team, Inchon 406840, South Korea
Han, M. K.
Kim, Hansung
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Yonsei Univ, Dept Chem & Biomol Engn, Seoul 120749, South KoreaKorea Inst Ind Technol KITECH, Surface Technol Team, Inchon 406840, South Korea
Kim, Hansung
Shul, Yong-Gun
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Yonsei Univ, Dept Chem & Biomol Engn, Seoul 120749, South KoreaKorea Inst Ind Technol KITECH, Surface Technol Team, Inchon 406840, South Korea
Shul, Yong-Gun
Jung, Kyeong Taek
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机构:Korea Inst Ind Technol KITECH, Surface Technol Team, Inchon 406840, South Korea