High pressure gas processing configurations and methods
View Patent ↗Contemplated plants comprise an acid gas removal unit that receives a compressed gas from an injection gas compressor, wherein acid gas is removed from the compressed gas in the acid gas removal unit at a pressure approximately above pipeline pressure.
1. A plant comprising an acid gas removal unit that receives a portion of dehydrated and C5 + depleted gas from an injection gas compressor at a pressure above a pipeline pressure, wherein the dehydrated and C5 + depleted gas comprises a sales gas and an acid gas, and wherein the acid gas is removed by a physical solvent or a chemical solvent in the acid gas removal unit.
2. The plant of claim 1 wherein the dehydrated and C5 + depleted gas has a carbon dioxide content of at least 10 mol % and a water dew point of about −40° F.
3. The plant of claim 2 wherein the dehydrated and C5 + depleted gas is further C4 + depleted.
4. The plant of claim 1 wherein the physical solvent is selected from the group of propylene carbonate, a morpholine solvent, and a dimethylether of polyethylene glycol, and wherein the chemical solvent comprises MDEA.
5. The plant of claim 1 wherein the pipeline pressure is at least 2300 psig.
6. The plant of claim 1 wherein the dehydrated and C5 + depleted gas is let down in pressure to about pipeline pressure before the acid gas is removed in the acid gas removal unit.
7. The plant of claim 1 wherein the dehydrated and C5 + depleted gas is let down in a turbo expander to a pressure at which the acid gas removal unit operates.
8. The plant of claim 7 wherein the pressure at which the acid gas removal unit operates is lower than the pipeline pressure.
9. The plant of claim 8 wherein the C5 + depleted gas that leaves the acid gas removal unit is compressed to the pipeline pressure by power generated from the turbo expander.
10. The plant of claim 8 wherein the C5 + depleted gas that leaves the acid gas removal unit is used as a refrigerant.
11. The plant of claim 1 further comprising a bypass that receives a portion of the dehydrated and C5 + depleted gas from the injection gas compressor at a pressure above pipeline pressure, and wherein the portion of the dehydrated and C5 + depleted gas is injected to a reservoir formation.
12. The plant of claim 11 wherein the portion of the dehydrated and C5 + depleted gas is up to 100% of a total flow rate of the dehydrated and C5 + depleted gas.
13. The plant of claim 1 wherein the acid gas that is removed by the acid gas removal unit is compressed and injected to a reservoir formation.
14. A plant comprising:
an injection gas compression unit that receives a dehydrated gas comprising an acid gas and compresses the dehydrated gas to an injection pressure, thereby forming a compressed gas;
an acid gas removal unit that receives a first portion of the compressed gas, wherein at least some of the acid gas is removed in the acid gas removal unit at at least pipeline pressure using a physical solvent or chemical solvent to form a sales gas; and
wherein the sales gas is fed to a pipeline, the removed acid gas is compressed and injected to a reservoir formation, and wherein optionally a second portion of the compressed gas is injected to the reservoir formation for disposal or enhanced oil recovery.
15. The plant of claim 14 wherein the dehydrated gas is C5 + depleted, has a carbon dioxide content of at least 10 mol %, and a water dew point of about −40° F.
16. The plant of claim 14 wherein the pipeline pressure is at least 2300 psig.
17. The plant of claim 14 wherein the physical solvent is selected from the group of propylene carbonate, a ruorpholine solvent, and a dimethylether of polyethylene glycol.
18. The plant of clam 14 wherein the first portion of the compressed injection gas is let down in pressure to about pipeline pressure, and wherein the second portion of the compressed gas has a pressure above pipeline pressure.
19. A plant comprising:
a hydrocarbon source that provides at a production rate a crude hydrocarbon product and an associated gas comprising a sales gas and an acid gas;
an injection gas compression unit receiving and compressing at least a portion of the associated gas, thereby producing a compressed associated gas;
an acid gas removal unit fluidly coupled to the injection gas compression unit and receiving at least part of the compressed associated gas via JT valve or turbo expander, thereby separating the acid gas from the sales gas; and
a bypass fluidly coupled to the injection gas compression unit and receiving a portion of the compressed associated gas and thereby rendering the production rate of the crude hydrocarbon product independent from a flow rate of the sales gas.
20. The plant of claim 19 further comprising a oil/gas production facility in which the associated gas is dehydrated and C5+ depleted to form a treated gas with a carbon dioxide content of at least 10mol % and a water dew point of about −40° F.
21. The plant of claim 20 wherein the injection gas compression unit compresses the treated gas to a pressure above a sales gas pipeline pressure.
22. The plant of claim 21 wherein the pressure above sales gas pipeline pressure is at least 3500 psig.
23. The plant of claim 19 wherein the acid gas removal unit operates at a pressure of about sales gas pipeline pressure.
24. The plant of claim 19 wherein the acid gas removal unit operates at a pressure that is below a sales gas pipeline pressure.
25. The plant of claim 19 wherein the acid gas removal unit employs a physical solvent or chemical solvent to remove at least a portion of the acid gas.