Biomass-enhanced natural gas from coal formations
US-10151185-B2 · Dec 11, 2018 · US
US9810050B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9810050-B2 |
| Application number | US-201214358687-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 16, 2012 |
| Priority date | Dec 20, 2011 |
| Publication date | Nov 7, 2017 |
| Grant date | Nov 7, 2017 |
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Methods and systems for enhanced recovery of coal bed methane. A method includes generating a diluent gas mixture comprising N 2 and CO 2 in a semi-closed Brayton cycle power plant, injecting at least a portion of the diluent gas mixture into a coal bed, and recovering a mixed production gas comprising methane from the coal bed.
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What is claimed is: 1. A method for enhanced recovery of coalbed methane, comprising: compressing a gaseous fuel for use in a semi-closed Brayton cycle power plant; generating a gas mixture comprising N 2 and CO 2 in the semi-closed Brayton cycle power plant operating to combust the gaseous fuel and an oxygen component of an oxidant at a stoichiometric ratio; injecting at least a portion of the gas mixture into a coal bed; and recovering a mixed production gas comprising methane from the coal bed. 2. The method of claim 1 , comprising completing an injection well in a coal bed. 3. The method of claim 1 , comprising completing a production well in a coal bed. 4. The method of claim 1 , comprising compressing the gas mixture prior to injection. 5. The method of claim 1 , comprising using at least a portion of the mixed production gas to fuel the semi-closed Brayton cycle power plant. 6. The method of claim 1 , comprising recovering heat energy from an exhaust generated by the semi-closed Brayton cycle power plant in a heat recovery steam generator (HRSG). 7. The method of claim 6 , comprising generating power with steam generated in the HRSG. 8. The method of claim 1 , comprising processing the mixed production gas to remove acid gases and water vapor to generate a natural gas capable of transport by pipeline. 9. The method of claim 8 , comprising liquefying the natural gas. 10. The method of claim 1 , comprising cooling the gas mixture prior to injection into the coal bed. 11. The method of claim 10 , comprising recovering heat from the gas mixture to supply process heat to a facility. 12. The method of claim 1 , wherein the oxidant for the semi-closed Brayton cycle power plant is air. 13. The method of claim 1 , wherein the oxidant used in the semi-closed Brayton cycle power plant has an oxygen concentration greater than about 21% by volume. 14. A system for enhancing the recovery of coalbed methane, comprising: a semi-closed Brayton cycle power plant operating to combust a gaseous fuel and an oxygen component of an oxidant at a stoichiometric ratio, wherein an exhaust gas from the semi-closed Brayton cycle power plant provides a diluent gas mixture comprising substantial amounts of N 2 and CO 2 ; a compressor configured to compress the gaseous fuel prior to combustion in the semi-closed Brayton cycle power plant; an injection well configured to inject the diluent gas mixture from the semi-closed Brayton cycle power plant into a coalbed; and a production well configured to harvest a production gas mixture from the coal bed, wherein the production gas mixture comprises methane. 15. The system of claim 14 , comprising a heat recovery steam generator configured to use an exhaust heat from the semi-closed Brayton cycle power plant to generate steam. 16. The system of claim 15 , comprising a power plant configured to use the steam to generate electricity. 17. The system of claim 14 , comprising a gas separation system configured to generate a CO 2 rich gas stream and a CO 2 lean gas stream. 18. The system of claim 17 , comprising injecting the CO 2 rich gas stream into the coalbed. 19. The system of claim 14 , comprising a liquefied natural gas plant configured to use electricity generated by the semi-closed Brayton cycle power plant to power a liquefaction process. 20. A system for enhancing the recovery of coalbed methane, comprising: a combustor associated with a gas turbine, the combustor configured to combust therein a gaseous fuel and an oxygen component of an oxidant at a stoichiometric ratio, wherein the gas turbine receives hot exhaust gases from the combustor, wherein cooling is provided by a diluent gas injected into the combustor, and wherein the diluent gas substantially comprises N 2 and CO 2 ; a generator configured to convert mechanical energy provided by the gas turbine into electrical energy; a heat recovery steam generator (HRSG) configured to generate steam by heating a boiler with an exhaust stream from the gas turbine; a Rankine cycle power plant configured to generate electricity from the steam; a cooler configured to condense water from the exhaust stream downstream of the HRSG, generating the diluent; a diluent compressor configured to increase the pressure of the diluent and direct at least a portion of the diluent to the combustor; an injection system configured to inject a portion of the diluent from the compressor into a coalbed; a production system configured to harvest a production gas from the coalbed, wherein the production gas comprises methane; and a compressor configured to compress a portion of the production gas to generate a compressed stream of coal bed methane, wherein a portion of the compressed stream of coal bed methane is used as part of the gaseous fuel. 21. The system of claim 20 , comprising a desalination unit integrated into the HRSG that is configured to produce a fresh water stream. 22. The system of claim 20 , comprising a pipeline configured to convey another portion of the compressed stream of coal bed methane to a market. 23. The system of claim 20 , wherein at least a portion of the electricity from the power plant is used to power facilities associated with the production gas.
the fuel or oxidant being gaseous at standard temperature and pressure (F02C3/28 takes precedence) · CPC title
Enhanced recovery methods for obtaining hydrocarbons · CPC title
Production of coal-bed methane (E21B43/243 takes precedence) · CPC title
with exhaust fluid of one cycle heating the fluid in another cycle (F01K17/025 takes precedence) · CPC title
using the exhaust gases of gas-turbines · CPC title
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