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A process for the removal of inert gases, such as nitrogen and carbon dioxide, from methane-containing gases, such as natural gas, including a first stage removal which lowers the total combined inert content to about less than 30% and a second stage removal utilizing a pressure swing adsorption pro

A process for the removal of inert gases, such as nitrogen and carbon dioxide, from methane-containing gases, such as natural gas, including a first stage removal which lowers the total combined inert content to about less than 30% and a second stage removal utilizing a pressure swing adsorption process comprising one or more adsorbent beds comprising contracted titanosilicate-1 adsorbent, wherein the purified methane-containing gas contains less than about 6% total combined inerts.

대표청구항 ▼

What is claimed is: 1. A process to purify a natural gas stream comprising between about 25% and 60% total inerts, the process comprising the steps of: (a) treating the natural gas stream with a first stage process comprising one or more processes of the group of selective membrane filtration, cryo

What is claimed is: 1. A process to purify a natural gas stream comprising between about 25% and 60% total inerts, the process comprising the steps of: (a) treating the natural gas stream with a first stage process comprising one or more processes of the group of selective membrane filtration, cryogenic distillation and amine scrubbing to produce a semi-purified natural gas stream comprising less than or equal to about 30% total combined inerts; and (b) treating the semi-purified natural gas stream with a second stage process in a pressure swing adsorption unit having one or more adsorbent beds having CTS-1 molecular sieve to obtain a product natural gas stream comprising less than about 5% total combined inerts. 2. The process of claim 1 wherein the natural gas stream is a raw produced natural gas. 3. The process of claim 1 wherein the inerts consist essentially of nitrogen and carbon dioxide. 4. The process of claim 1 wherein the first stage process is selective membrane filtration comprising a nitrogen selective membrane. 5. The process of claim 1 wherein the first stage process comprises selective membrane filtration with a carbon dioxide selective membrane. 6. The process of claim 1 wherein the first stage process comprises cryogenic distillation. 7. The process of claim 1 wherein the first stage process comprises an amine scrubbing process. 8. The process of claim 4 wherein methane permeates the nitrogen selective membrane. 9. The process of claim 5 wherein carbon dioxide permeates the carbon dioxide selective membrane. 10. The process of claim 4 or 5 wherein the first stage process comprises more than one membrane connected in series. 11. The process of claim 2 wherein the product gas is a pipeline quality natural gas. 12. The process of claim 1 wherein the second stage is operated at pressures between about 100 and 800 psig. 13. An integrated synthetic hydrocarbon production process comprising the process of claim 1. 14. The method of claim 1 wherein the natural gas stream is natural gas associated with oil production. 15. A process to produce a pipeline quality natural gas comprising the steps of: (a) compressing a nitrogen-rich raw natural gas produced at low pressure to a first pressure between about 400 and about 1,000 psia to form a compressed feed gas stream; (b) feeding the compressed feed gas stream at a temperature greater than about 40�� C. to the feed side of a membrane filtration system wherein the membrane is more permeable to methane than to nitrogen to produce a semi-purified stream; (c) recovering from the permeate side of the membrane, at a second pressure lower than the first pressure, a first permeate gas stream comprising less than or equal to about 30% nitrogen; (d) recompressing the first permeate gas stream in a second stage feed gas booster compressor to produce a pressure swing adsorption feed gas; and (e) recovering from the outlet of the membrane feed side a non-permeate gas stream enriched in nitrogen as compared to the compressed feed gas stream. 16. The process of claim 15 further comprising the steps of: (f) feeding the non-permeate gas to the feed side of a second membrane filtration system; and (g) recovering from the permeate side of the second membrane filtration system, at a third pressure lower than the first pressure, a second permeate gas stream reduced in nitrogen content compared to the first step membrane non-permeate gas stream. 17. The process of claim 15 wherein the second pressure is between about 25 and about 300 psia. 18. The process of claim 16 wherein the third pressure is greater than about 25 psia. 19. The process of claim 16 further comprising the step of: (h) recycling the second permeate gas stream to the raw feed gas or the compressed feed gas stream. 20. The process of claim 19 further comprising the step of: (i) withdrawing the second permeate stream as a fuel stream. 21. The process of claim 1 wherein the natural gas is associated with oil production; wherein the first stage is a carbon dioxide selective membrane filtration; and further comprising the step of recovering the permeate stream which consists essentially of carbon dioxide. 22. The process of claim 1 wherein the adsorbent is mixed with one or more materials selected from the group of clays, silicas, and metal oxides. 23. The process of claim 15 wherein the adsorbent is mixed with one or more materials selected from the group of clays, silicas, and metal oxides.