Hydrogen Production via Synthetic Gas by Biomass/Oil Partial Oxidation

0371543 - ÚCHP 2012 RIV NL eng J - Článek v odborném periodiku
Hanika, Jiří - Lederer, J. - Tukač, V. - Veselý, Václav - Kováč, D.
Hydrogen Production via Synthetic Gas by Biomass/Oil Partial Oxidation.
Chemical Engineering Journal. 176-177, - (2011), s. 286-290. ISSN 1385-8947. E-ISSN 1873-3212.
[International Conference on Chemical Reactors CHEMREACTOR-19 /19./. Vienna, 05.09.2010-09.09.2010]
Grant CEP: GA MPO 2A-2TP1/024
Výzkumný záměr: CEZ:AV0Z40720504
Klíčová slova: hydrogen * biomass * partial oxidation
Kód oboru RIV: CI - Průmyslová chemie a chemické inženýrství
Impakt faktor: 3.461, rok: 2011

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.
Trvalý link: http://hdl.handle.net/11104/0205035