Volume 34, Issue 2 pp. 307-317
Research Article

Analysis of Methanol Production from Biomass Gasification

W. Feng

W. Feng

Department of Biochemical Engineering, Beijing University of Chemical Technology, Beijing, China

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P. Ji

Corresponding Author

P. Ji

Department of Chemical Engineering, Beijing University of Chemical Technology, Beijing, China

Department of Chemical Engineering, Beijing University of Chemical Technology, Beijing, ChinaSearch for more papers by this author
B. Chen

B. Chen

Department of Chemical Engineering, Beijing University of Chemical Technology, Beijing, China

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D. Zheng

D. Zheng

Department of Chemical Engineering, Beijing University of Chemical Technology, Beijing, China

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First published: 24 January 2011
Citations: 25

Abstract

A biomass-based methanol production process was investigated. The process consists of a biomass gasifier, steam reformer, and methanol synthesis reactor as the main units. Reactors were simulated by applying the kinetic models previously developed and the process was analyzed based on the simulation results. The key parameters, the equivalence ratio in biomass gasification, the temperature in steam reforming, and the recycle of hydrogen in methanol synthesis were identified. These parameters affect the methanol production. The process analysis indicates that the optimal combinations of the parameters can greatly enhance the methanol production and the thermodynamic efficiency. Finally, the elemental analysis for carbon and hydrogen along the process was carried out.

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