초록 ▼

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

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.

대표청구항 ▼

What is claimed is: 1. A process comprising: obtaining produced gas from a source of produced gas, said produced gas including hydrocarbon gas and carbon dioxide; cooling said produced gas to a temperature below zero degrees Fahrenheit to form cooled produced gas; providing a fractionation tower an

What is claimed is: 1. A process comprising: obtaining produced gas from a source of produced gas, said produced gas including hydrocarbon gas and carbon dioxide; cooling said produced gas to a temperature below zero degrees Fahrenheit to form cooled produced gas; providing a fractionation tower and introducing said cooled produced gas into said fractionation tower to form a first stream and a second stream, said first stream including said hydrocarbon gas and a first portion of said carbon dioxide gas and said second stream being a liquid including the remainder of the carbon dioxide; supplying said first stream to a methanol removal system and processing said first stream through said methanol removal system to form a stream of injectable carbon dioxide gas from said first stream and a stream of hydrocarbon gas as a first process output; supplying said injectable stream of carbon dioxide gas to said fractionation tower and injecting said injectable stream of carbon dioxide gas into said fractionation tower for combination with carbon dioxide in said tower being formed into said second stream; and supplying said second stream as a waste output. 2. The process of claim 1 further including pressurizing said second stream, connecting said second stream to an injection well and injecting said stream into said injection well. 3. The process of claim 2 further wherein said injectable stream of carbon dioxide gas is send through a heat exchanger before injection into said fractionation tower. 4. The process of claim 3 wherein said produced gas includes nitrogen and, helium, wherein said hydrocarbon is methane and wherein said first stream includes said nitrogen, said helium and said methane, and wherein said first process output is fractionated into a sales stream that includes said methane, into a stream that includes said helium and a stream that includes said nitrogen. 5. The process of claim 4 wherein said produced gas is first dehydrated and then cooled to below 30 degrees below zero Fahrenheit and provided at a pressure of about 660 pounds per square inch. 6. A process comprising: obtaining produced gas from a source of produced gas, said produced gas including hydrocarbon gas, hydrogen sulfide and carbon dioxide; cooling said produced gas to a temperature below zero degrees Fahrenheit to form cooled produced gas; providing a fractionation tower and introducing said cooled produced gas into said fractionation tower to form a first stream and a second stream, said first stream including said hydrocarbon gas and a first portion of said carbon dioxide gas, and said second stream being a liquid and including the hydrogen sulfide and the remainder of the carbon dioxide; supplying said first stream to a methanol removal system with methanol and operating said methanol removal system to combine said methanol with the carbon dioxide in said first stream to form a stream of methanol and carbon dioxide liquid and a stream of said hydrocarbon gas as a first process output; operating said methanol recovery system to separate said methanol and said carbon dioxide to form an injectable stream of carbon dioxide; supplying said injectable stream of carbon dioxide to said fractionation tower and injecting said injectable stream of carbon dioxide into said fractionation tower for combination with carbon dioxide in said tower being formed into said second stream; and supplying said second stream as a second process output. 7. The process of claim 6 wherein said produced gas is first dehydrated and then cooled to below 30 degrees below zero Fahrenheit. 8. The process of claim 7 wherein said injectable stream of carbon dioxide is cooled before it is injected into said fractionation tower. 9. The process of claim 5 wherein said methanol removal system is operated so that said first process output is at a temperature of below zero degrees Fahrenheit. 10. The product of the process of claim 9. 11. The product of the process of claim 5. 12. A process comprising: obtaining produced gas from a source of produced gas, said produced gas including hydrocarbon gas and carbon dioxide; cooling said produced gas to a temperature below zero degrees Fahrenheit to form cooled produced gas; providing a fractionation tower and introducing said cooled produced gas into said fractionation tower to form a first stream and a second stream, said first stream including said hydrocarbon gas and a first portion of said carbon dioxide gas and said second stream being a liquid including the remainder of the carbon dioxide; supplying said first stream to a chemical removal system and processing said first stream through said chemical removal system to form a stream of injectable carbon dioxide gas from said first stream and a stream of hydrocarbon gas-as a first process output; supplying said injectable stream of carbon dioxide gas to said fractionation tower and injecting said injectable stream of carbon dioxide gas into said fractionation tower for combination with carbon dioxide in said tower being formed into said second stream; and supplying said second stream as a waste output. 13. The process of claim 12 wherein said chemical removal system is a methanol removal system. 14. The process of claim 12 further including pressurizing said second stream, connecting said second stream to an injection well and injecting said stream into said injection well. 15. The process of claim 12 further wherein said injectable stream of carbon dioxide gas is cooled before injection into said fractionation tower.