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Hydrogen Production via Synthetic Gas by Biomass/Oil Partial Oxidation
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SYSNO ASEP 0371543 Document Type J - Journal Article R&D Document Type Journal Article Subsidiary J Článek ve WOS Title Hydrogen Production via Synthetic Gas by Biomass/Oil Partial Oxidation Author(s) Hanika, Jiří (UCHP-M) RID, ORCID, SAI
Lederer, J. (CZ)
Tukač, V. (CZ)
Veselý, Václav (UCHP-M) RID, SAI
Kováč, D. (CZ)Source Title Chemical Engineering Journal. - : Elsevier - ISSN 1385-8947
176-177, - (2011), s. 286-290Number of pages 5 s. Action International Conference on Chemical Reactors CHEMREACTOR-19 /19./ Event date 05.09.2010-09.09.2010 VEvent location Vienna Country AT - Austria Event type EUR Language eng - English Country NL - Netherlands Keywords hydrogen ; biomass ; partial oxidation Subject RIV CI - Industrial Chemistry, Chemical Engineering R&D Projects 2A-2TP1/024 GA MPO - Ministry of Industry and Trade (MPO) CEZ AV0Z40720504 - UCHP-M (2005-2011) UT WOS 000298900200039 DOI 10.1016/j.cej.2011.06.050 Annotation Comparison of pilot plant partial oxidation of meal rape and hydrocarbon oil mixture with process simulation using equilibrium reactor model by process simulator Aspen Plus resulted in a good agreement. The application of representative compounds method for simulation of such complex mixture was found as a useful tool for optimal process conditions prediction. Based on this procedure the ratio feed to both oxygen and steam were proposed for prediction of good experimental parameters for good process yield of hydrogen. It was stated that key parameter lambda (or analogously oxygen to feed ratio) controlling the partial oxidation process in optimal regime should be in the interval 0.6–0.8, i.e. under reduction conditions. Workplace Institute of Chemical Process Fundamentals Contact Eva Jirsová, jirsova@icpf.cas.cz, Tel.: 220 390 227 Year of Publishing 2012
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