Abstract

A concept for combined hydrogen and power production from natural gas with CO2 capture is presented. The process involves the use of a metal oxide in fluidized bed reactors; the metal oxide is reduced by a mixture of natural gas and steam in a fuel reactor and oxidized by air in the air reactor. The natural gas is partially oxidized in the fuel reactor, resulting in a mixture of CO2, H2, H2O, and CO from the exit. If no hydrocarbons are present in this stream, it can be sent to a water gas shift reactor to get an undiluted stream of CO2 and H2. The product stream from the air reactor contains mostly N2 and some unreacted oxygen. The oxidation reaction is exothermic with resulting heat production in the air reactor; this heat is used to maintain the oxygen carrier particles at the high temperature necessary for the endothermic reaction in the fuel reactor. The hot gases from the air reactor could be used for power production. Metal oxides of Ni, Cu, Mn, and Fe were prepared by impregnation on a SiO2 suppor...

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