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This paper presents technical aspects of hydrogen production technology through co-gasification of coal and biomass based on modeling and simulation of the process. Three plant configurations containing entrained-flow gasifiers were studied. A performance analysis regarding the energy efficiency of the process, carbon conversion rate and the carbon dioxide capture rate have been carried out. A significant advantage of gasification process described in this paper is the limitations of greenhouse gas emissions through acid gas removal unit (carbon dioxide capture, hydrogen sulfide processing).

Keywords: hydrogen production, gasification, entrained-flow reactors, energy efficiency, CO2 capture and storage