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US 2013/0095029 A1Published application
Co-production of methanol and ammonia
AssigneeHaldor Topsoe A/S
InventorPat A. Han
Life of this patent
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Abstract
Process for the co-production of methanol and ammonia from a hydrocarbon feed without venting to the atmosphere carbon dioxide captured from the methanol or ammonia synthesis gas and without using expensive air separation units, water gas shift and acid gas wash for removal of carbon.
Claims9
Process for co-producing methanol and ammonia from a hydrocarbon feedstock comprising the sequential steps of:
- (a) producing a methanol synthesis gas containing hydrogen, carbon oxides and nitrogen by steam reforming the hydrocarbon feedstock in a primary reforming stage and subsequently in an air-blown secondary reforming stage;
- (b) splitting the methanol synthesis gas into a first methanol synthesis gas stream containing 1-50 vol % of the methanol synthesis gas and a second methanol synthesis gas stream containing 50-99 vol % of the methanol synthesis gas stream, forming a first methanol synthesis gas stream with reduced content of carbon dioxide by passing the first methanol synthesis gas stream through a CO2 Pressure Swing Adsorption (CO2 PSA) while bypassing the second methanol synthesis gas stream, withdrawing an off-gas stream containing hydrogen, carbon dioxide, carbon monoxide and methane from the CO2 Pressure Swing Adsorption, and forming a combined methanol synthesis gas by mixing the first methanol stream with reduced content of carbon dioxide with the by-passed second methanol synthesis stream;
- (c) catalytically converting the carbon oxides and hydrogen of the combined methanol synthesis gas in a once-through methanol synthesis stage and withdrawing an effluent containing methanol and a gas effluent containing nitrogen, hydrogen and unconverted carbon oxides;
- (d) producing an ammonia synthesis gas by methanation of unconverted carbon oxides of the gas effluent of step (c) in a catalytic methanation stage and withdrawing an ammonia synthesis gas having a H2:N2 molar ratio of 3:1 without the use of water gas shift and without further use of carbon dioxide removal;
- (e) catalytically converting the nitrogen and hydrogen of the ammonia synthesis gas in an ammonia synthesis stage and withdrawing an effluent containing ammonia and an off-gas stream containing hydrogen, nitrogen and methane.
2 more elements
Dependencies are inferred from the claim text.