초록 ▼

The present disclosure provides a method for separating and purifying a landfill gas stream. In one embodiment, the method includes a step of collecting a crude landfill gas stream which includes at least methane, carbon dioxide, oxygen, and nitrogen gases. The method also includes a step of separat

The present disclosure provides a method for separating and purifying a landfill gas stream. In one embodiment, the method includes a step of collecting a crude landfill gas stream which includes at least methane, carbon dioxide, oxygen, and nitrogen gases. The method also includes a step of separating the crude landfill gas stream into at least an intermediate landfill gas stream and a first waste gas stream using a membrane separation unit, wherein the intermediate landfill gas stream is enriched in methane and depleted in carbon dioxide relative to the crude landfill gas stream. The method further includes a step of separating the intermediate landfill gas stream into at least a final landfill gas stream and a second waste gas stream using a pressure swing adsorption separation unit, wherein the final landfill gas stream is enriched in methane and depleted in carbon dioxide, oxygen, and nitrogen relative to the intermediate landfill gas stream. In some embodiments. VOCs in the waste gas streams are destroyed using a thermal oxidizer.

대표청구항 ▼

What is claimed is: 1. A method for separating and purifying a landfill gas stream, the method comprising the steps of: collecting a crude landfill gas stream which includes at least methane, carbon dioxide, oxygen, and nitrogen gases; separating the crude landfill gas stream into at least an inter

What is claimed is: 1. A method for separating and purifying a landfill gas stream, the method comprising the steps of: collecting a crude landfill gas stream which includes at least methane, carbon dioxide, oxygen, and nitrogen gases; separating the crude landfill gas stream into at least an intermediate landfill gas stream and a first waste gas stream using a membrane separation unit, wherein the intermediate landfill gas stream is enriched in methane and depleted in carbon dioxide relative to the crude landfill gas stream and the first waste gas stream comprises volatile organic compounds separating the intermediate landfill gas stream into at least a final landfill gas stream and a second waste gas stream using a pressure swing adsorption separation unit, wherein the final landfill gas stream is enriched in methane and depleted in carbon dioxide, oxygen, and nitrogen relative to the intermediate landfill gas stream; and treating the first waste gas stream in a thermal oxidizer unit to substantially destroy the volatile organic compounds therein so that the first waste gas stream may be released into the atmosphere. 2. The method of claim 1, wherein the crude landfill gas stream comprises from about 45 to about 55 mole percent methane, from about 20 to about 40 mole percent carbon dioxide, and from about 5 to about 20 mole percent nitrogen. 3. The method of claim 1, wherein the final landfill gas stream comprises at least about 96 mole percent methane, no more than about 1 mole percent carbon dioxide, and no more than about 4 mole percent nitrogen. 4. The method of claim 1, wherein the second waste gas stream comprises volatile organic compounds and wherein the method further comprises a step of treating the second waste gas stream in the thermal oxidizer unit to substantially destroy the volatile organic compounds therein so that the second waste gas stream may be released into the atmosphere. 5. The method of claim 1, wherein at least a portion of the crude landfill gas stream is separated into a first recycle gas stream using the membrane separation unit and wherein the first recycle gas stream is recombined with the crude landfill gas stream. 6. The method of claim 5, wherein the first recycle gas stream comprises from about 30 to about 40 mole percent of the crude landfill gas stream. 7. The method of claim 1, wherein at least a portion of the intermediate landfill gas stream is separated into a second recycle gas stream using the pressure swing adsorption separation unit and wherein the second recycle gas stream is recombined with the crude landfill gas stream. 8. The method of claim 7, wherein the second recycle gas stream comprises from about 17 to about 22 mole percent of the intermediate landfill gas stream. 9. The method of claim 1, wherein the crude landfill gas stream further includes hydrogen sulfide gas and wherein the method further comprising a step of removing at least a portion of the hydrogen sulfide gas from the crude landfill gas stream before the crude landfill gas stream is separated using the membrane separation unit. 10. The method of claim 1, wherein the crude landfill gas stream further includes oxygen, water vapor, and volatile organic compounds and wherein the final landfill gas stream is depleted in oxygen, water vapor, and volatile organic compounds relative to the crude landfill gas stream. 11. A system for separating and purifying a landfill gas stream comprising: a feed gas conduit in flow communication with a crude landfill gas stream which includes at least methane, carbon dioxide, oxygen, and nitrogen gases; a membrane separation unit in flow communication with the feed gas conduit for separating the crude landfill gas stream into at least an intermediate landfill gas stream and a first waste gas stream, wherein the intermediate landfill gas stream is enriched in methane and depleted in carbon dioxide relative to the crude landfill gas stream; a pressure swing adsorption separation unit in flow communication with the membrane separation unit for receiving the intermediate landfill gas stream therefrom and separating the intermediate landfill gas stream into at least a final landfill gas stream and a second waste gas stream, wherein the final landfill gas stream is enriched in methane and depleted in carbon dioxide, oxygen, and nitrogen relative to the intermediate landfill gas stream; and a thermal oxidizer unit in flow communication with the membrane separation unit for receiving the first waste gas stream, wherein the first waste gas stream comprises volatile organic compounds and wherein the thermal oxidizer unit substantially destroys the volatile organic compounds in the first waste gas stream so that the first waste gas stream may be released into the atmosphere. 12. The system of claim 11, wherein the crude landfill gas stream comprises from about 45 to about 55 mole percent methane, from about 20 to about 40 mole percent carbon dioxide, and from about 5 to about 20 mole percent nitrogen. 13. The system of claim 11, wherein the final landfill gas stream comprises at least about 96 mole percent methane, no more than about 1 mole percent carbon dioxide, and no more than about 4 mole percent nitrogen. 14. The system of claim 11, wherein the thermal oxidizer unit is further in flow communication with the pressure swing adsorption unit for receiving the second waste gas stream, wherein the second waste gas stream comprises volatile organic compounds and wherein the thermal oxidizer unit substantially destroys the volatile organic compounds in the second waste gas stream so that the second waste gas stream may be released into the atmosphere. 15. The system of claim 11, further comprising a recycle conduit in flow communication with the membrane separation unit, wherein at least a portion of the crude landfill gas stream is separated into a first recycle gas stream using the membrane separation unit and wherein the first recycle gas stream is recombined with the crude landfill gas stream via the recycle conduit. 16. The system of claim 15, wherein the first recycle gas stream comprises from about 30 to about 40 mole percent of the crude landfill gas stream. 17. The system of claim 11, further comprising a recycle conduit in flow communication with the pressure swing adsorption unit, wherein at least a portion of the intermediate landfill gas stream is separated into a second recycle gas stream using the pressure swing adsorption separation unit and wherein the second recycle gas stream is recombined with the crude landfill gas stream via the recycle conduit. 18. The system of claim 17, wherein the second recycle gas stream comprises from about 17 to about 22 mole percent of the intermediate landfill gas stream. 19. The system of claim 11, wherein the crude landfill gas stream further includes hydrogen sulfide gas and wherein the system further comprises a hydrogen sulfide separation unit in flow communication with the crude landfill gas stream for removing at least a portion of the hydrogen sulfide gas from the crude landfill gas stream before the crude landfill gas stream is separated using the membrane separation unit. 20. The system of claim 11, wherein the crude landfill gas stream further includes oxygen, water vapor, and volatile organic compounds and wherein the final landfill gas stream is depleted in oxygen, water vapor, and volatile organic compounds relative to the crude landfill gas stream. 21. A method for separating and purifying a landfill gas stream, the method comprising the steps of: collecting a crude landfill gas stream which includes at least methane, carbon dioxide, oxygen, and nitrogen gases; separating the crude landfill gas stream into at least an intermediate landfill gas stream and a first waste gas stream using a membrane separation unit, wherein the intermediate landfill gas stream is enriched in methane and depleted in carbon dioxide relative to the crude landfill gas stream; and separating the intermediate landfill gas stream into at least a final landfill gas stream and a second waste gas stream using a pressure swing adsorption separation unit, wherein the final landfill gas stream is enriched in methane and depleted in carbon dioxide, oxygen, and nitrogen relative to the intermediate landfill gas stream and the second waste gas stream comprises volatile organic compounds; and treating the second waste gas stream in a thermal oxidizer unit to substantially destroy the volatile organic compounds therein so that the second waste gas stream may be released into the atmosphere. 22. The method of claim 21, wherein the crude landfill gas stream comprises from about 45 to about 55 mole percent methane, from about 20 to about 40 mole percent carbon dioxide, and from about 5 to about 20 mole percent nitrogen. 23. The method of claim 21, wherein the final landfill gas stream comprises at least about 96 mole percent methane, no more than about 1 mole percent carbon dioxide, and no more than about 4 mole percent nitrogen. 24. The method of claim 21, wherein at least a portion of the crude landfill gas stream is separated into a first recycle gas stream using the membrane separation unit and wherein the first recycle gas stream is recombined with the crude landfill gas stream. 25. The method of claim 24, wherein the first recycle gas stream comprises from about 30 to about 40 mole percent of the crude landfill gas stream. 26. The method of claim 21, wherein at least a portion of the intermediate landfill gas stream is separated into a second recycle gas stream using the pressure swing adsorption separation unit and wherein the second recycle gas stream is recombined with the crude landfill gas stream. 27. The method of claim 26, wherein the second recycle gas stream comprises from about 17 to about 22 mole percent of the intermediate landfill gas stream. 28. The method of claim 21, wherein the crude landfill gas stream further includes hydrogen sulfide gas and wherein the method further comprising a step of removing at least a portion of the hydrogen sulfide gas from the crude landfill gas stream before the crude landfill gas stream is separated using the membrane separation unit. 29. The method of claim 21, wherein the crude landfill gas stream further includes oxygen, water vapor, and volatile organic compounds and wherein the final landfill gas stream is depleted in oxygen, water vapor, and volatile organic compounds relative to the crude landfill gas stream. 30. A system for separating and purifying a landfill gas stream comprising: a feed gas conduit in flow communication with a crude landfill gas stream which includes at least methane, carbon dioxide, oxygen, and nitrogen gases; a membrane separation unit in flow communication with the feed gas conduit for separating the crude landfill gas stream into at least an intermediate landfill gas stream and a first waste gas stream, wherein the intermediate landfill gas stream is enriched in methane and depleted in carbon dioxide relative to the crude landfill gas stream; a pressure swing adsorption separation unit in flow communication with the membrane separation unit for receiving the intermediate landfill gas stream therefrom and separating the intermediate landfill gas stream into at least a final landfill gas stream and a second waste gas stream, wherein the final landfill gas stream is enriched in methane and depleted in carbon dioxide, oxygen, and nitrogen relative to the intermediate landfill gas stream; and a thermal oxidizer unit in flow communication with the pressure swing adsorption unit for receiving the second waste gas stream, wherein the second waste gas stream comprises volatile organic compounds and wherein the thermal oxidizer unit substantially destroys the volatile organic compounds in the second waste gas stream so that the second waste gas stream may be released into the atmosphere. 31. The system of claim 30, wherein the crude landfill gas stream comprises from about 45 to about 55 mole percent methane, from about 20 to about 40 mole percent carbon dioxide, and from about 5 to about 20 mole percent nitrogen. 32. The system of claim 30, wherein the final landfill gas stream comprises at least about 96 mole percent methane, no more than about 1 mole percent carbon dioxide, and no more than about 4 mole percent nitrogen. 33. The system of claim 30, further comprising a recycle conduit in flow communication with the membrane separation unit, wherein at least a portion of the crude landfill gas stream is separated into a first recycle gas stream using the membrane separation unit and wherein the first recycle gas stream is recombined with the crude landfill gas stream via the recycle conduit. 34. The system of claim 33, wherein the first recycle gas stream comprises from about 30 to about 40 mole percent of the crude landfill gas stream. 35. The system of claim 30, further comprising a recycle conduit in flow communication with the pressure swing adsorption unit, wherein at least a portion of the intermediate landfill gas stream is separated into a second recycle gas stream using the pressure swing adsorption separation unit and wherein the second recycle gas stream is recombined with the crude landfill gas stream via the recycle conduit.