Methods of vapor pressure stabilization of crude oil
View Patent ↗Methods of crude oil stabilization may include separating crude oil in a bulk separator into a first light hydrocarbon stream, a first water stream, and a first bottoms stream; separating the first bottoms stream in an intermediate pressure separator into a second light hydrocarbon stream, a second water stream, and a second bottoms stream; separating the second bottoms stream in a separator into a third light hydrocarbon stream, a third water stream, and a third bottoms stream; introducing a stripping gas stream comprising methane into the separator; storing the third bottoms stream in a vessel comprising an outlet for a fourth light hydrocarbon stream; treating at least a portion of the first, second, third, and fourth light hydrocarbon streams in a vapor treatment process to form a final light hydrocarbon stream; and recycling at least a portion of the final light hydrocarbon stream to the separator.
1 . A method comprising:
separating a multi-phase crude oil in a bulk separator into a first light hydrocarbon stream, a first water stream, and a first bottoms stream;
separating the first bottoms stream in an intermediate pressure separator into a second light hydrocarbon stream, a second water stream, and a second bottoms stream;
separating the second bottoms stream in a separator into a third light hydrocarbon stream, a third water stream, and a third bottoms stream;
introducing a stripping gas stream comprising methane into the separator;
storing the third bottoms stream in a vessel comprising an outlet for a fourth light hydrocarbon stream;
treating at least a portion of the first, second, third, and fourth light hydrocarbon streams in a vapor treatment process to form a final light hydrocarbon stream; and
recycling at least a portion of the final light hydrocarbon stream to the separator as at least a portion of the stripping gas stream.
2 . The method of claim 1 , wherein the bulk separator operates at a temperature of about 70° F. to about 130° F.
3 . The method of claim 1 , wherein the bulk separator operates at a pressure of about 100 psig to about 150 psig.
4 . The method of claim 1 , wherein the intermediate pressure separator operates at a temperature of about 70° F. to about 130° F.
5 . The method of claim 1 , wherein the intermediate pressure separator operates at a pressure of about 30 psig to about 50 psig.
6 . The method of claim 1 , wherein the separator operates at a temperature of about 70° F. to about 130° F.
7 . The method of claim 1 , wherein the separator has an electric heater operably coupled thereto to heat the separator to a temperature of about 90° F. to about 140° F.
8 . The method of claim 1 , wherein the separator operates at a pressure of about 0.5 psig to about 10 psig.
9 . The method of claim 1 , wherein the separator comprises a gas-liquid separator, a vapor recovery tower, a stripping tower, or any combination thereof.
10 . The method of claim 1 , wherein the third light hydrocarbon stream comprises a higher concentration of C 2 -C 5 hydrocarbons than the stripping gas stream.
11 . The method of claim 1 , wherein the stripping gas stream comprises about 90 mol % methane or more.
12 . The method of claim 1 , wherein the third bottoms stream has a Reid vapor pressure of about 7 psia to about 12 psia.
13 . The method of claim 1 , wherein the vapor treatment process comprises a natural gas liquids recovery unit.
14 . The method of claim 13 , wherein the natural gas liquids recovery unit comprises a cryogenic processing unit, a fuel gas conditioning skid, a membrane unit, or any combination thereof.
15 . The method of claim 1 , further comprising compressing one or more of the first light hydrocarbon stream, the second light hydrocarbon stream, the third light hydrocarbon stream, or the fourth hydrocarbon stream in the vapor treatment process by a compressor.
16 . The method of claim 1 , wherein the separator comprises trays, packing, or any combination thereof to enhance separation.
17 . A method comprising:
separating a multi-phase crude oil in a bulk separator into a first light hydrocarbon stream, a first water stream, and a first bottoms stream;
separating the first bottoms stream in an intermediate pressure separator into a second light hydrocarbon stream, a second water stream, and a second bottoms stream;
separating the second bottoms stream in a separator into a third light hydrocarbon stream, a third water stream, and a third bottoms stream;
introducing a stripping gas stream comprising methane into the separator;
storing the third bottoms stream in a vessel comprising an outlet for a fourth light hydrocarbon stream; and
slipping at least a portion of the first light hydrocarbon stream to the separator as at least a portion of the stripping gas stream.
18 . The method of claim 17 , further comprising treating at least a portion of the first, second, third, and fourth light hydrocarbon streams in a vapor treatment process to form a final light hydrocarbon stream.