Gas stripping process for removal of sulfur-containing components from crude oil
High rate gas stripping for removal of sulfur-containing components such as mercaptans from crude oil may be conducted by feeding sweet gas to the bottom of a tower containing pre-heated mercaptan-containing crude oil feed. The gas bubbles up through the crude becoming enriched with H 2 S, mercaptans, CO 2 and/or hydrocarbons. The rich gas exits the tower, and is treated to produce a sweetened gas, a portion of which is recycled to the tower, and an acid gas. The remainder of the sweetened and/or the acid gas may be used as a fuel or processed to recover a portion of any hydrocarbons that may have been stripped out of the crude oil with the mercaptans, sulfur-containing components, CO 2 , used for enhanced oil recovery or disposed.
1. A method for reducing sulfur containing compounds and specifically the mercaptan content of a mercaptan containing crude oil stream where the method for reducing the mercaptan content of the crude oil stream consisting essentially of stripping the mercaptan containing crude oil stream with a gas stream having a relatively reduced level of mercaptans to produce a gas stream containing an increased level of mercaptans and a crude oil stream containing a reduced level of mercaptans in a non-reactive system, and wherein the method involves an absence of hydrogenation as a means of removing sulfur containing compounds from the crude oil stream.
2. The method of claim 1 where the gas stream strips the mercaptans from the mercaptan containing crude oil stream at a high rate where the high rate is between about 0.1 to about 1.0 MSCF per barrel of crude oil (about 18 to about 180 m 3 gas/m 3 ).
3. The method of claim 1 where the total amount of sulfur-containing components in the crude oil stream is reduced to a level of about 40 ppmw or below.
4. The method of claim 1 where the stripping is conducted in a tower where the hydrocarbon stream is introduced at or near the top of the tower, the gas stream is introduced at or near the bottom of the tower, the gas containing sulfur-containing components is removed at or near the top of the tower and the hydrocarbon stream containing reduced level of sulfur-containing component is removed at or near the bottom of the tower.
5. The method of claim 1 further comprising separating liquid from the gas stream containing an increased level of sulfur-containing components and contacting the resulting gas stream with a solvent to remove at least a portion of the sulfur-containing components therefrom.
6. The method of claim 5 further comprising splitting the resulting gas stream into a relatively higher molecular weight hydrocarbon fraction and a relatively lower molecular weight hydrocarbon fraction.
7. The method of claim 1 wherein the stripping is conducted by a technique selected from the group consisting of cocurrent contact, countercurrent contact, cross-current contact and combinations thereof.
8. The method of claim 1 wherein the stripping is conducted in the presence of packing.
9. The method of claim 1 where the stripping is conducted in the presence of trays.
10. The method of claim 1 wherein the gas stream strips methyl mercaptan, ethyl mercaptan and mixtures thereof from the crude oil stream.
11. The method of claim 10 where the gas stream is sweet natural gas.
12. The method of claim 2 where the gas stream rate is at least about 0.25 MSCF per barrel of crude oil (about 44 m 3 gas/m 3 crude oil).
13. The method of claim 12 where the gas stream rate is at least about 0.3 MSCF per barrel of crude oil (about 53 m 3 gas/m 3 crude oil).
14. The method of claim 1 where the crude oil stream is heated to a temperature no higher than about 350° F. for the stripping.
15. A method for reducing the sulfur containing compounds and specifically the mercaptan content of a mercaptan containing crude oil stream where the method for reducing the mercaptan content of the crude oil stream consists essentially of stripping the mercaptan containing crude oil stream with a gas stream having a relatively reduced level of mercaptans to produce a gas stream containing an increased level of mercaptans and a crude oil stream containing a reduced level of mercaptans in a non-reactive system, and wherein the method involves an absence of hydrogenation as a means of removing sulfur containing compounds from the crude oil stream, wherein the gas stream strips methyl mercaptan, ethyl mercaptan and mixtures thereof from the crude oil stream, and wherein the gas stream strips the mercaptans from the mercaptan containing crude oil stream at a high rate where the high rate is between about 0.1 to about 1.0 MSCF per barrel of crude oil (about 18 to about 180 m 3 gas/m 3 ).
16. The method of claim 15 where the crude oil stream is heated to a temperature no higher than about 350° F. for the stripping.
17. The method of claim 15 further including separating liquid from the gas stream containing an increased level of sulfur-containing components and contacting the resulting gas stream with a solvent to remove at least a portion of the sulfur-containing components therefrom.