Separation of a sour syngas stream
A feed stream, comprising hydrogen sulphide (H 2 S), carbon dioxide (CO 2 ), hydrogen (H 2 ) and, optionally, carbon monoxide (CO), is separated into at least a CO 2 product stream and an H 2 or H 2 and CO product stream. The stream is separated using a pressure swing adsorption system, an H 2 S removal system and a further separation system, which systems are used in series to separate the stream. The method has particular application in the separation of a sour (i.e. sulphur containing) syngas, as for example produced from the gasification of solid or heavy liquid carbonaceous feedstock.
1. A method for separating a feed stream, comprising at least H 2 S, CO and H 2 , into at least a CO 2 product stream and an H 2 or H 2 and CO product stream (the “H 2 /CO product stream”), wherein the feed stream is formed from a sour syngas stream obtained from gasification of a solid or liquid carbonaceous feedstock and is separated using a pressure swing adsorption system (the “H 2 /CO-PSA system”), an H 2 S removal system, and a further separation system, and wherein:
the feed stream is introduced into either the H 2 /CO-PSA system or the H 2 S removal system;
the H 2 /CO-PSA system either separates the feed stream to provide the H 2 /CO product stream and a stream enriched in CO 2 and H 2 S, or separates a stream already depleted in H 2 S by the H 2 S removal system to provide the H 2 /CO product stream and a stream enriched in CO 2 and depleted in H 2 S;
the H 2 S removal system either processes the feed stream to provide a stream depleted in H 2 S, or processes a stream already enriched in CO 2 and H 2 S by the H 2 /CO-PSA system to provide a stream enriched in CO 2 and depleted in H 2 S, or processes a stream already enriched in CO 2 and H 2 S by the H 2 /CO-PSA system and further enriched in CO 2 and H 2 S by the further separation system to provide the CO 2 product stream; and
the further separation system either separates a stream already enriched in CO 2 and H 2 S by the H 2 /CO-PSA system to provide a stream further enriched in CO 2 and H 2 S and a stream comprising H 2 or H 2 and CO, or separates a stream already enriched in CO 2 by the H 2 /CO-PSA system and depleted in H 2 S by the H 2 S removal system to provide the CO 2 product stream and a stream comprising H 2 or H 2 and CO.
2. The method of claim 1 , wherein the H 2 S removal system separates the feed stream, or said stream already enriched in CO 2 and H 2 S by the H 2 /CO-PSA system, or said stream already enriched in CO 2 and H 2 S by the H 2 /CO-PSA system and further enriched in CO 2 and H 2 S by the further separation system, to provide an H 2 S enriched stream in addition to providing said stream depleted in H 2 S, said stream enriched in CO 2 and depleted in H 2 S, or said CO 2 product stream.
3. The method of claim 2 , wherein the H 2 S removal system is another pressure swing adsorption system (the “sour-PSA system”).
4. The method of claim 1 , wherein the further separation system is a partial condensation system.
5. The method of claim 1 , wherein the further separation system is a membrane separation system.
6. The method of claim 1 , wherein the feed stream comprises from about 500 ppm to about 5 mole % H 2 S, from about 10 to about 60 mole % CO 2 , and from about 35 mole % to the remainder of H 2 or a mixture of H 2 and CO.
7. The method of claim 1 , wherein at least about 80% of the H 2 present in the feed stream is recovered in the H 2 /CO product stream and at most about 25% of the CO 2 present in the feed stream is recovered the H 2 /CO product stream, and wherein the H 2 /CO product stream contains at most about 50 ppm H 2 S.
8. The method of claim 1 , wherein at least about 75% of the H 2 and CO present in the feed stream is recovered the H 2 /CO product stream and at most about 25% of the CO 2 present in the feed stream is recovered the H 2 /CO product stream, and wherein the H 2 /CO product stream contains at most about 50 ppm H 2 S.
9. The method of claim 1 , wherein the CO 2 product stream has a CO 2 concentration of at least about 90 mole % and contains at most about 100 ppm H 2 S.
10. The method of claim 2 , wherein the H 2 S enriched stream has a H 2 S concentration of from about 20 to about 80 mol %.
11. The method of claim 1 , wherein some or all of the stream comprising H 2 or H 2 and CO obtained from the further separation system is recycled to the H 2 /CO-PSA system for further separation.
12. The method of claim 1 , wherein some or all of the stream comprising H 2 or H 2 and CO obtained from the further separation system is combusted to generate power.
13. The method of claim 1 , wherein some or all of the stream comprising H 2 or H 2 and CO obtained from the further separation system is combusted in the presence of sufficient O 2 to convert all or substantially all of the H 2 and CO in the part of the stream combusted to H 2 O and CO 2 .
14. The method of claim 3 , wherein steam is used as a purge gas for purging the sour-PSA.
15. The method of claim 3 , wherein some or all of the stream comprising H 2 or H 2 and CO obtained from the further separation system is used as a purge gas for purging the sour-PSA.
16. The method of claim 1 , wherein:
the feed stream is introduced into the H 2 /CO-PSA system;
the H 2 /CO-PSA system separates the feed stream to provide the H 2 /CO product stream and a stream enriched in CO 2 and H 2 S;
the H 2 S removal system processes said stream enriched in CO 2 and H 2 S to provide a stream enriched in CO 2 and depleted in H 2 S; and
the further separation system separates said stream enriched in CO 2 and depleted in H 2 S to provide the CO 2 product stream and a stream comprising H 2 or H 2 and CO.
17. The method of claim 16 , wherein feed stream further comprises water, and the H 2 S removal system processes said stream enriched in CO 2 and H 2 S to provide a stream enriched in CO 2 and depleted in H 2 S and water.
18. The method of claim 1 , wherein:
the feed stream is introduced into the H 2 S removal system;
the H 2 S removal system processes the feed stream to provide a stream depleted in H 2 S;
the H 2 /CO-PSA system separates said stream depleted in H 2 S to provide the H 2 /CO product stream and a stream enriched in CO 2 and depleted in H 2 S; and
the further separation system separates said stream enriched in CO 2 and depleted in H 2 S to provide the CO 2 product stream and a stream comprising H 2 or H 2 and CO.
19. The method of claim 18 , wherein feed stream further comprises water, and the H 2 S removal system processes the feed stream to provide a stream depleted in H 2 S and water.
20. The method of claim 1 , wherein:
the feed stream is introduced into the H 2 /CO-PSA system;
the H 2 /CO-PSA system separates the feed stream to provide the H 2 /CO product stream and a stream enriched in CO 2 and H 2 S;
the further separation system separates said stream enriched in CO 2 and H 2 S to provide a stream further enriched in CO 2 and H 2 S and a stream comprising H 2 or H 2 and CO;
the H 2 S removal system processes said stream further enriched in CO 2 and H 2 S to provide the CO 2 product stream.
21. Apparatus for separating a feed stream, formed from a sour syngas stream obtained from gasification of a solid or liquid carbonaceous feedstock and comprising at least H 2 S, CO 2 and H 2 , into at least a CO 2 product stream and an H 2 or H 2 and CO product stream (the “H 2 /CO product stream”), the apparatus comprising:
a pressure swing adsorption system (the “H 2 /CO-PSA system”) for separating the feed stream to provide the H 2 /CO product stream and a stream enriched in CO 2 and H 2 S;
a conduit arrangement for introducing the feed stream into the H 2 /CO-PSA system;
a conduit arrangement for withdrawing the H 2 /CO product stream from the H 2 /CO-PSA system;
an H 2 S removal system, for processing said stream enriched in CO 2 and H 2 S to provide a stream enriched in CO 2 and depleted in H 2 S;
a conduit arrangement for withdrawing the stream enriched in CO 2 and H 2 S from the H 2 /CO-PSA system and introducing the stream into the H 2 S removal system;
a further separation system, for separating said stream enriched in CO 2 and depleted in H 2 S to provide the CO 2 product stream and a stream comprising H 2 or H 2 and CO;
a conduit arrangement for withdrawing the stream enriched in CO 2 and depleted in H 2 S from the H 2 S removal system and introducing the stream into the further separation system;
a conduit arrangement for withdrawing the CO 2 product stream from the further separation system; and
a conduit arrangement for withdrawing the stream comprising H 2 or H 2 and CO from the further separation system.
22. Apparatus for separating a feed stream, formed from a sour syngas stream obtained from gasification of a solid or liquid carbonaceous feedstock and comprising at least H 2 S, CO 2 and H 2 , into at least a CO 2 product stream and an H 2 or H 2 and CO product stream (the “H 2 /CO product stream”), the apparatus comprising:
an H 2 S removal system, for processing the feed stream to provide a stream depleted in H 2 S;
a conduit arrangement for introducing the feed stream into the H 2 S removal system;
a pressure swing adsorption system (the “H 2 /CO-PSA system”) for separating said stream depleted in H 2 S to provide the H 2 /CO product stream and a stream enriched in CO 2 and depleted in H 2 S;
a conduit arrangement for withdrawing the stream depleted in H 2 S from the H 2 S removal system and introducing the stream into the H 2 /CO-PSA system;
a conduit arrangement for withdrawing the H 2 /CO product stream from the H 2 /CO-PSA system;
a further separation system, for separating said stream enriched in CO 2 and depleted in H 2 S to provide the CO 2 product stream and a stream comprising H 2 or H 2 and CO;
a conduit arrangement for withdrawing the stream enriched in CO 2 and depleted in H 2 S from the H 2 /CO-PSA system and introducing the stream into the further separation system;
a conduit arrangement for withdrawing the CO 2 product stream from the further separation system; and
a conduit arrangement for withdrawing the stream comprising H 2 or H 2 and CO from the further separation system.
23. Apparatus for separating a feed stream, formed from a sour syngas stream obtained from gasification of a solid or liquid carbonaceous feedstock and comprising at least H 2 S, CO 2 and H 2 , into at least a CO 2 product stream and an H 2 or H 2 and CO product stream (the “H 2 /CO product stream”), the apparatus comprising:
a pressure swing adsorption system (the “H 2 /CO-PSA system”) for separating the feed stream to provide the H 2 /CO product stream and a stream enriched in CO 2 and H 2 S;
a conduit arrangement for introducing the feed stream into the H 2 /CO-PSA system;
a conduit arrangement for withdrawing the H 2 /CO product stream from the H 2 /CO-PSA system;
a further separation system, for separating said stream enriched in CO 2 and H 2 S to provide a stream further enriched in CO 2 and H 2 S and a stream comprising H 2 or H 2 and CO;
a conduit arrangement for withdrawing the stream enriched in CO 2 and H 2 S from the H 2 /CO-PSA system and introducing the stream into the further separation system;
a conduit arrangement for withdrawing the stream comprising H 2 or H 2 and CO from the further separation system;
an H 2 S removal system, for processing said stream further enriched in CO 2 and H 2 S to provide the CO 2 product stream;
a conduit arrangement for withdrawing the stream further enriched in CO 2 and H 2 S from the further separation system and introducing the stream into the H 2 S removal system; and
a conduit arrangement for withdrawing the CO 2 product stream from the H 2 S removal system.