Expander and method for co2 separation
Abstract
In one aspect an expander for separating carbon dioxide (CO 2 ) from a gas stream is presented. The expander includes (a) a housing; (b) at least one rotating component disposed within the housing; (c) at least one inlet disposed in the housing, wherein the inlet is configured to receive the gas stream;(d) at least one first outlet disposed in the housing, wherein the first outlet is configured to discharge a CO 2 rich stream; and (e) at least one second outlet disposed in the housing, wherein the second outlet is configured to discharge a CO 2 lean stream. The expander is configured to cool the gas stream such that a portion of CO 2 in the gas stream forms one or both of solid CO 2 and liquid CO 2 . The expander is further configured to separate at least a portion of one or both of solid CO 2 and liquid CO 2 from the gas stream to form the CO 2 rich stream and the CO 2 lean stream. System and method for separating carbon dioxide (CO 2 ) from a gas stream are also presented
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . An expander for separating carbon dioxide (CO 2 ) from a gas stream, comprising:
(a) a housing; (b) at least one rotating component disposed within the housing; (c) at least one inlet disposed in the housing, wherein the inlet is configured to receive the gas stream; (d) at least one first outlet disposed in the housing, wherein the first outlet is configured to discharge a CO 2 rich stream; and (e) at least one second outlet disposed in the housing, wherein the second outlet is configured to discharge a CO 2 lean stream;
wherein the expander is configured to cool the gas stream such that a portion of CO 2 in the gas stream forms one or both of solid CO 2 and liquid CO 2 , and
wherein the expander is further configured to separate at least a portion of one or both of solid CO 2 and liquid CO 2 from the gas stream to form the CO 2 rich stream and the CO 2 lean stream.
2 . The expander as defined in claim 1 , wherein the expander is configured to cool the gas stream such that a portion of CO 2 in the gas stream primarily forms solid CO 2 , and
wherein the expander is further configured to separate the solid CO 2 from the gas stream to form a solid CO 2 rich stream.
3 . The expander as defined in claim 1 , wherein the housing comprises one or more separation channels in fluid communication with the first outlet and configured to separate the CO 2 rich stream from the gas stream.
4 . The expander as defined in claim 1 , wherein the expander is configured to separate at least about 50 mass percent of CO 2 present in the gas stream.
5 . The expander as defined in claim 1 , wherein the CO 2 lean stream is substantially free of CO 2 .
6 . The expander as defined in claim 2 , wherein at least one component of the expander further comprises a coating configured to preclude adhesion of solid CO 2 to a surface of the expander component.
7 . The expander as defined in claim 2 , wherein the expander further comprises at least one heated component configured to preclude adhesion of solid CO 2 to a surface of the expander component.
8 . The expander as defined in claim 1 , further comprising at least one separator in fluid communication with the second outlet of the expander, wherein the at least one separator is configured to separate a portion of CO 2 in the CO 2 lean stream to form a supplementary CO 2 rich stream.
9 . The expander as defined in claim 1 , wherein the first outlet is disposed in the housing at a location upstream of the rotating component and the second outlet is disposed in the housing at a location downstream of the rotating component.
10 . A system for separating carbon dioxide (CO 2 ) from a gas stream, comprising:
(i) at least one compression stage and at least one cooling stage configured to compress and cool a gas stream; (ii) at least one expansion stage comprising at least one expander in fluid communication with the cooling stage or the compression stage, the expander comprising:
(a) a housing;
(b) at least one rotating component disposed within the housing;
(c) at least one inlet disposed in the housing, wherein the inlet is configured to receive the gas stream;
(d) at least one first outlet disposed in the housing, wherein the first outlet is configured to discharge a CO 2 rich stream; and
(e) at least one second outlet disposed in the housing, wherein the second outlet is configured to discharge a CO 2 lean stream;
wherein the expander is configured to cool the gas stream such that a portion of CO 2 in the gas stream forms one or both of solid CO 2 and liquid CO 2 , and
wherein the expander is further configured to separate at least a portion of one or both of solid CO 2 and liquid CO 2 from the gas stream to form the CO 2 rich stream and the CO 2 lean stream.
11 . The system as defined in claim 10 , wherein the expander is configured to cool the gas stream such that a portion of CO 2 in the gas stream primarily forms solid CO 2 , and
wherein the expander is further configured to separate the solid CO 2 from the gas stream to form a solid CO 2 rich stream.
12 . The system as defined in claim 11 , wherein at least one component of the expander further comprises a coating configured to preclude adhesion of solid CO 2 to a surface of the expander component.
13 . The system as defined in claim 11 , wherein the expander further comprises at least one heated component configured to preclude adhesion of solid CO 2 to a surface of the expander component.
14 . The system as defined in claim 10 , further comprising at least one separator in fluid communication with the second outlet of the expander,
wherein the at least one separator is configured to separate a portion of CO 2 in the CO 2 lean stream to form a supplementary CO 2 rich stream.
15 . A method of separating carbon dioxide (CO 2 ) from a gas stream, comprising:
(i) providing an expander, comprising:
(a) a housing;
(b) at least one rotating component disposed within the housing
(c) at least one inlet disposed in the housing, wherein the inlet is configured to receive the gas stream;
(d) at least one first outlet disposed in the housing, wherein the first outlet is configured to discharge a CO 2 rich stream; and
(e) at least one second outlet disposed in the housing, wherein the second outlet is configured to discharge a CO 2 lean stream;
(ii) cooling the gas stream in the expander such that a portion of CO 2 in the gas stream forms one or both of solid CO 2 and liquid CO 2 ; and (iii) separating at least a portion of one or both of solid CO 2 and liquid CO 2 from the gas stream in the expander to form the CO 2 rich stream and the CO 2 lean stream.
16 . The method as defined in claim 15 , wherein step (i) comprises cooling the gas stream in the expander to primarily form solid CO 2 and step (ii) comprises separating the solid CO 2 from the gas stream to form a solid CO 2 rich stream.
17 . The method as defined in claim 15 , wherein at least about 50 volume percent of CO 2 present in the gas stream is separated in step (ii).
18 . The method as defined in claim 15 , wherein the CO 2 lean stream is substantially free of CO 2 .
19 . The method as defined in claim 15 , wherein step (ii) comprises separating at least a portion of one or both of solid CO 2 and liquid CO 2 from the gas stream in the expander through one or more separation channels.
20 . The method as defined in claim 16 , wherein at least one component of the expander further comprises a coating configured to preclude adhesion of solid CO 2 to a surface of the expander component.
21 . The method as defined in claim 16 , further comprising heating at least one component of the expander to preclude adhesion of solid CO 2 to a surface of the expander component.Cited by (0)
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