Carbon dioxide and hydrogen sulfide recovery system using a combination of membranes and low temperature cryogenic separation processes
An acid gas purification system is described herein that includes a primary membrane system with a CO 2 - and H 2 S-enriched permeate stream effluent and a hydrocarbon stream effluent; a first compression stage arranged to receive the CO 2 - and H 2 S-enriched permeate stream and produce a compressed stream; and a cryogenic separation system to receive the compressed stream, the cryogenic separation system including a cooler followed by a fractionator, wherein the fractionator produces a CO 2 - and H 2 S liquid stream and a hydrocarbon gas stream.
1. An acid gas purification system, comprising:
a primary membrane system with a CO 2 - and H 2 S-enriched permeate stream effluent and a hydrocarbon stream effluent;
a first compressor arranged to receive the CO 2 - and H 2 S-enriched permeate stream and produce a compressed stream; and
a cryogenic separation system to receive the compressed stream,
the cryogenic separation system including a conditioner followed by a frozen CO 2 fractionator, wherein the frozen CO 2 fractionator comprises a stripping section, a rectification section, and a mid-section, wherein the mid-section comprises a side processor comprising an empty section configured to return a solid to the frozen CO 2 fractionator, and wherein the side processor further comprises a condenser that produces a liquid level in the side processor, and
wherein the frozen CO 2 fractionator produces a CO 2 and H 2 S liquid stream and a hydrocarbon gas stream, and the hydrocarbon gas stream is compressed in a second compressor and blended with the hydrocarbon stream effluent of the primary membrane system.
2. The acid gas purification system of claim 1 , wherein the fractionator produces a bottoms stream, and a portion of the bottoms stream is recycled to the first compressor.
3. The acid gas purification system of claim 1 , wherein the fractionator produces an overhead stream, and the hydrocarbon gas stream is obtained from the overhead stream.
4. The acid gas purification system of claim 1 , wherein the fractionator produces a reflux stream, and a portion of the reflux stream is recycled as a recycle stream, which is heat-integrated with the compressed stream.
5. The acid gas purification system of claim 4 , wherein the recycle stream is compressed in the second compressor and blended with the hydrocarbon stream effluent of the primary membrane system.
6. The acid gas purification system of claim 5 , wherein the fractionator produces a bottoms stream, and a portion of the bottoms stream is recycled to the first compressor.
7. An acid gas purification system, comprising:
a membrane separation unit that produces a permeate stream enriched in CO 2 and/or H 2 S and a retentate stream from a feed stream;
a conditioner to reduce a temperature of the permeate stream; and
a cryogenic fractionator to separate acid gases from the cooled permeate stream, the cryogenic fractionator having an overhead that is compressed and blended with the retentate stream,
wherein the cryogenic fractionator is a frozen CO 2 fractionator comprising a stripping section, a rectification section, and a mid-section, wherein the mid-section comprises a side processor comprising an empty section configured to return a solid to the frozen CO 2 fractionator, and wherein the side processor further comprises a condenser that produces a liquid level in the side processor.
8. The acid gas purification system of claim 7 , wherein the permeate stream is at least 95 mol % CO 2 and/or H 2 S.
9. The acid gas purification system of claim 7 , wherein the cryogenic fractionator produces a bottoms stream, and a portion of the bottoms stream is recycled to the conditioner.
10. The acid gas purification system of claim 7 , wherein the cryogenic fractionator produces a reflux stream, and a portion of the reflux stream is recycled as a recycle stream, which is heat-integrated with the conditioner.
11. The acid gas purification system of claim 7 , wherein the membrane separation unit is a polymer membrane unit.
12. An acid gas purification system, comprising:
a non-distillation separation system with an acid gas effluent and a separation gas effluent, wherein the non-distillation separation system is a single step separation and the acid gas effluent is at least 90 mol % CO 2 and/or H 2 S; and
a cryogenic fractionation system including a conditioner and a fractionator, wherein the cryogenic fractionation system produces an overhead stream that is compressed and blended with the separation gas effluent of the non-distillation separation system,
wherein the fractionator is a frozen CO 2 fractionator comprising a stripping section, a rectification section, and a mid-section, wherein the mid-section comprises a side processor comprising an empty section configured to return a solid to the frozen CO 2 fractionator, and wherein the side processor further comprises a condenser that produces a liquid level in the side processor.
13. The acid gas purification system of claim 12 , wherein the non-distillation separation system is one or more of a membrane system, a pressure swing adsorption system, and a solvent extraction system.
14. The acid gas purification system of claim 12 , wherein the cryogenic fractionation system produces a bottoms stream, and a portion of the bottoms stream is recycled to the conditioner.