System for separating carbon dioxide and hydrocarbon gas from a produced gas combined with nitrogen
View Patent ↗Produced natural gas containing carbon dioxide is dehydrated and chilled to liquefy the carbon dioxide and then fractionated to produce a waste stream of liquid carbon dioxide and hydrogen sulfide. Natural gas liquids may be first separated and removed before fractionation. After fractionation, the waste stream is pressurized and transmitted to a remote injection well for injection either for disposal of the waste stream and preferably to urge hydrocarbons toward the producing well. A hydrocarbon stream proceeds from fractionation to a methanol absorber system which removes carbon dioxide gas. The hydrocarbon stream is thereafter separated into at least hydrocarbon gas, nitrogen and helium. Some of the nitrogen is reintroduced into a fractionation tower to enhance the recovery of hydrocarbons. A methanol recovery system is provided to recover and reuse the methanol. The hydrocarbons are sold as natural gas and the helium is recovered and sold. Excess nitrogen is vented.
1. A process comprising:
obtaining produced gas from a source of produced gas, said produced gas including methane and carbon dioxide;
separating the produced gas into a first stream and a second stream, said first stream including at least said methane and a first portion of said carbon dioxide as a gas and said second stream including at least a second portion of said carbon dioxide processed into a liquid;
providing a source of nitrogen and supplying nitrogen from said source for combination with the produced gas being separated into said first stream and said second stream;
processing said first stream to separate said carbon dioxide as a gas and said methane;
returning said carbon dioxide as a gas for incorporation with said produced gas;
supplying said methane as a first output; and
supplying said second stream as a second output.
2. The process of claim 1 wherein said processing of said produced gas includes fractionating said produced gas into said first stream and said second stream in a fractionating tower having a top and a bottom, and wherein said stream of nitrogen is introduced into said fractionating tower proximate to said bottom and wherein said first stream is removed from said fractionating tower proximate to said top.
3. The process of claim 2 wherein said first stream is supplied to an absorber system and wherein said absorber system is operated to remove said carbon dioxide as a gas from said first stream.
4. The process of claim 3 wherein said absorber system includes methanol, and wherein said methanol is combined with said first stream to combine with said carbon dioxide as a gas, and wherein said methanol with said carbon dioxide as a gas is processed to separate said carbon dioxide as a gas from said methanol.
5. The process of claim 4 wherein said second stream is pressurized and supplied to an injection well.
6. The process of claim 3 wherein said first stream includes said methane and at least nitrogen and wherein said first stream is fractionated to an output of said hydrocarbon gas and an output of said nitrogen.
7. The process of claim 6 wherein said output of said nitrogen is said source of nitrogen.