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Volumn 62, Issue 4, 2007, Pages 1239-1250

Experimental demonstration of the reverse flow catalytic membrane reactor concept for energy efficient syngas production. Part 1: Influence of operating conditions

Author keywords

Chemical reactors; Experimental; Membranes; Packed bed; Partial oxidation; Syngas

Indexed keywords

HEAT LOSSES; MEMBRANES; PACKED BEDS; PRESSURE DROP; SYNTHESIS GAS; SYSTEMS ANALYSIS;

EID: 33845906619     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.ces.2006.10.009     Document Type: Article
Times cited : (11)

References (16)
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    • Gosiewski K., Bartmann U., Moszczynski M., and Mleczko L. Effect of the intraparticle mass transport limitations on temperature profiles and catalytic performance of the reverse-flow reactor for the partial oxidation of methane to synthesis gas. Chemical Engineering Science 54 20 (1999) 4589-4602
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    • Feasibility study of a reverse flow catalytic membrane reactor with porous membranes for the production of syngas
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    • Smit, J., Zhang, W., van Sint Annaland, M., Kuipers, J. A. M., 2007. Feasibility study of a novel membrane reactor for syngas production. part 2: adiabatic reactor simulations. Journal of Membrane Science, accepted for publication.
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* 이 정보는 Elsevier사의 SCOPUS DB에서 KISTI가 분석하여 추출한 것입니다.