A simulation model of homogeneous combustion of air-methane mixture in a fluidized bed composed of inert particles was established. This model, based on the assumptions of the bubble assemblage model, accounts for the thermal exchanges between phases and the radiating exchange with the wall. The experimental study was performed on a pilot fluidized-bed reactor 180 mm in diameter, fitted axially with sampling probes for analysing the gas composition. For bed temperature ranging between 850 and 950 degrees C, the comparison of the measured gas compositions and the theoretical results showed a good agreement as regards the methane conversion rate along the bed. (C) 1998 Elsevier Science Ltd. All rights reserved.
机构:
Institute of Engineering Thermophysics, Chinese Academy of Sciences, Beijing 100190, ChinaInstitute of Engineering Thermophysics, Chinese Academy of Sciences, Beijing 100190, China
Lu, Qing-Gang
Liu, Qi
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Institute of Engineering Thermophysics, Chinese Academy of Sciences, Beijing 100190, China
Graduate School, Chinese Academy of Sciences, Beijing 100190, ChinaInstitute of Engineering Thermophysics, Chinese Academy of Sciences, Beijing 100190, China
Liu, Qi
Fan, Xiao-Xu
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机构:
Institute of Engineering Thermophysics, Chinese Academy of Sciences, Beijing 100190, China
Graduate School, Chinese Academy of Sciences, Beijing 100190, ChinaInstitute of Engineering Thermophysics, Chinese Academy of Sciences, Beijing 100190, China
Fan, Xiao-Xu
Song, Guo-Liang
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机构:
Institute of Engineering Thermophysics, Chinese Academy of Sciences, Beijing 100190, ChinaInstitute of Engineering Thermophysics, Chinese Academy of Sciences, Beijing 100190, China
Song, Guo-Liang
Na, Yong-Jie
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机构:
Institute of Engineering Thermophysics, Chinese Academy of Sciences, Beijing 100190, ChinaInstitute of Engineering Thermophysics, Chinese Academy of Sciences, Beijing 100190, China
Na, Yong-Jie
He, Jun
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Institute of Engineering Thermophysics, Chinese Academy of Sciences, Beijing 100190, ChinaInstitute of Engineering Thermophysics, Chinese Academy of Sciences, Beijing 100190, China
He, Jun
Kung Cheng Je Wu Li Hsueh Pao/Journal of Engineering Thermophysics,
2008,
29
(08):
: 1435
-
1439
机构:
Univ Carlos III Madrid, ISE Res Grp, Thermal & Fluid Engn Dept, Madrid 28911, SpainUniv Carlos III Madrid, ISE Res Grp, Thermal & Fluid Engn Dept, Madrid 28911, Spain
Sanchez-Delgado, S.
Marugan-Cruz, C.
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Univ Carlos III Madrid, ISE Res Grp, Thermal & Fluid Engn Dept, Madrid 28911, SpainUniv Carlos III Madrid, ISE Res Grp, Thermal & Fluid Engn Dept, Madrid 28911, Spain
Marugan-Cruz, C.
Soria-Verdugo, A.
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Univ Carlos III Madrid, ISE Res Grp, Thermal & Fluid Engn Dept, Madrid 28911, SpainUniv Carlos III Madrid, ISE Res Grp, Thermal & Fluid Engn Dept, Madrid 28911, Spain
Soria-Verdugo, A.
Santana, D.
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Univ Carlos III Madrid, ISE Res Grp, Thermal & Fluid Engn Dept, Madrid 28911, SpainUniv Carlos III Madrid, ISE Res Grp, Thermal & Fluid Engn Dept, Madrid 28911, Spain
机构:
China Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R ChinaChina Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
Liang, Yongshi
Zhang, Yongmin
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China Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R ChinaChina Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
Zhang, Yongmin
Li, Tingwen
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URS Corp, Morgantown, WV 26505 USAChina Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
Li, Tingwen
Lu, Chunxi
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China Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R ChinaChina Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China