Water gas shift reaction process
AssigneeJohnson Matthey PLC
InventorsGraham Charles Hinton, Richard Ian Johnston, John David Pach, Hsing-Chuan Yang, Ian Richard Barton
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AssigneeJohnson Matthey PLC
InventorsGraham Charles Hinton, Richard Ian Johnston, John David Pach, Hsing-Chuan Yang, Ian Richard Barton
Estimating the term…
A process for increasing the hydrogen content of a synthesis gas including hydrogen and carbon oxides and having a carbon monoxide content ≧45 mole % on a dry-gas basis, including the steps of: (i) combining the synthesis gas with steam to form a steam-enriched feed gas mixture (ii) passing the feed gas mixture at an inlet temperature in the range 220-370° C. over an iron-based water-gas shift catalyst to form a hydrogen-enriched shifted gas mixture having a carbon monoxide content ≦10 mole % on a dry gas basis, and (iii) recovering the hydrogen-enriched shifted gas mixture, where a portion of the hydrogen-enriched shifted gas mixture is recycled to the feed gas mixture.
A process for increasing the hydrogen content of a synthesis gas derived from the gasification of coal, petroleum coke or biomass, said synthesis gas comprising hydrogen and carbon oxides and having a carbon monoxide content ≧45 mole % on a dry-gas basis, comprising the steps of:
(canceled)
Dependencies are inferred from the claim text.