Processes for the separation of methane from a gas stream
First Claim
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1. A process for converting a carbonaceous feedstock into a plurality of gaseous products contained in a gas stream, and for separating hydrogen and methane from the gas stream, the process comprising the steps of:
- (a) supplying a carbonaceous feedstock to a gasification reactor, wherein the carbonaceous feedstock includes a carbon source selected from the group consisting of coal, petroleum coke, asphaltene, liquid petroleum residue, biomass and mixtures thereof;
(b) reacting the carbonaceous feedstock in the gasification reactor in the presence of steam and a gasification catalyst and under suitable temperature and pressure to form a first gas stream comprising methane, hydrogen, carbon monoxide, carbon dioxide, and one or more additional gaseous by-products;
(c) removing a substantial portion of the carbon dioxide and a substantial portion of the one or more additional gaseous by-products from the first gas stream to produce a second gas stream comprising methane, hydrogen, and optionally carbon monoxide;
(d) at least partially separating hydrogen from the second gas stream to form a hydrogen-enriched gas stream and a hydrogen-depleted gas stream, wherein the hydrogen-depleted gas stream comprises methane, optionally carbon monoxide and up to about 4 mol % hydrogen;
wherein, if the heating value of the hydrogen-depleted gas stream is less than 950 btu/scf (dry basis), and if the hydrogen-depleted gas stream comprises 1000 ppm or more of carbon monoxide;
(1) at least partially separating carbon monoxide from the hydrogen-depleted gas stream to form (i) a carbon monoxide-enriched gas stream and (ii) a methane-enriched gas stream having a heating value of at least 950 btu/scf (dry basis);
or (2) at least partially methanating the carbon monoxide in the hydrogen-depleted gas stream to form a methane-enriched gas stream.
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Abstract
Processes for the catalytic conversion of a carbonaceous composition into a gas stream comprising methane are provided. In addition, the processes provide for the generation of a hydrogen-enriched gas stream and, optionally, a carbon monoxide-enriched gas stream, which can be mixed or used separately as an energy source for subsequent catalytic gasification processes.
293 Citations
20 Claims
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1. A process for converting a carbonaceous feedstock into a plurality of gaseous products contained in a gas stream, and for separating hydrogen and methane from the gas stream, the process comprising the steps of:
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(a) supplying a carbonaceous feedstock to a gasification reactor, wherein the carbonaceous feedstock includes a carbon source selected from the group consisting of coal, petroleum coke, asphaltene, liquid petroleum residue, biomass and mixtures thereof; (b) reacting the carbonaceous feedstock in the gasification reactor in the presence of steam and a gasification catalyst and under suitable temperature and pressure to form a first gas stream comprising methane, hydrogen, carbon monoxide, carbon dioxide, and one or more additional gaseous by-products; (c) removing a substantial portion of the carbon dioxide and a substantial portion of the one or more additional gaseous by-products from the first gas stream to produce a second gas stream comprising methane, hydrogen, and optionally carbon monoxide; (d) at least partially separating hydrogen from the second gas stream to form a hydrogen-enriched gas stream and a hydrogen-depleted gas stream, wherein the hydrogen-depleted gas stream comprises methane, optionally carbon monoxide and up to about 4 mol % hydrogen; wherein, if the heating value of the hydrogen-depleted gas stream is less than 950 btu/scf (dry basis), and if the hydrogen-depleted gas stream comprises 1000 ppm or more of carbon monoxide;
(1) at least partially separating carbon monoxide from the hydrogen-depleted gas stream to form (i) a carbon monoxide-enriched gas stream and (ii) a methane-enriched gas stream having a heating value of at least 950 btu/scf (dry basis);
or (2) at least partially methanating the carbon monoxide in the hydrogen-depleted gas stream to form a methane-enriched gas stream.- View Dependent Claims (2, 3, 4, 5, 6)
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7. A process for converting a carbonaceous feedstock into a plurality of gaseous products contained in a gas stream, and for separating hydrogen and methane from the gas stream, the process comprising the steps of:
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(a) supplying a first carbonaceous feedstock to a reactor; (b) at least partially combusting the first carbonaceous feedstock in the reactor in the presence of oxygen and under suitable temperature and pressure so as to generate (i) heat energy and (ii) a combustion gas stream comprising hydrogen, carbon monoxide, and carbon dioxide; (c) using the heat energy from the combustion of the first carbonaceous feedstock to generate steam; (d) introducing at least a portion of the steam, at least a portion of the combustion gas stream, a second carbonaceous feedstock and a gasification catalyst to a gasification reactor, wherein the second carbonaceous feedstock includes a carbon source selected from the group consisting of coal, petroleum coke, asphaltene, liquid petroleum residue, biomass and mixtures thereof; (e) reacting the second carbonaceous feedstock in the gasification reactor in the presence of steam and the gasification catalyst under suitable temperature and pressure to form a first gas stream comprising methane, hydrogen, carbon monoxide, carbon dioxide and one or more additional gaseous by-products; (f) removing a substantial portion of the carbon dioxide and a substantial portion of the one or more gaseous by-products from the first gas stream to produce a second gas stream comprising methane, hydrogen and optionally carbon monoxide; (g) at least partially separating hydrogen from the second gas stream to form a hydrogen-enriched gas stream and a hydrogen-depleted gas stream, wherein the hydrogen-depleted gas stream comprises methane, optionally carbon monoxide and up to about 4 mol % hydrogen; wherein, if the heating value of the hydrogen-depleted gas stream is less than 950 btu/scf (dry basis), and if the hydrogen-depleted gas stream comprises 1000 ppm or more of carbon monoxide;
(1) at least partially separating carbon monoxide from the hydrogen-depleted gas stream to form (i) a carbon monoxide-enriched gas stream and (ii) a methane enriched gas stream having a heating value of at least 950 btu/scf (dry basis);
or (2) at least partially methanating the carbon monoxide in the hydrogen-depleted gas stream to form a methane-enriched gas stream.- View Dependent Claims (8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20)
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Specification