Monolayer, composite, gas separation material, filter, gas separation device and method for manufacturing composite
US-12128366-B2 · Oct 29, 2024 · US
US2016184771A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016184771-A1 |
| Application number | US-201514974355-A |
| Country | US |
| Kind code | A1 |
| Filing date | Dec 18, 2015 |
| Priority date | Dec 31, 2014 |
| Publication date | Jun 30, 2016 |
| Grant date | — |
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H 2 S is removed from a feed gas by a gas separation membrane including a separation layer that is made of a blend of P84 and Matrimid.
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What is claimed is: 1 . A method of removing H 2 S from a feed gas, comprising the steps of: feeding the feed gas comprising at least 2 vol % H 2 S to a feed gas inlet of a gas separation membrane apparatus that includes a composite fluid separation membrane, a permeate gas outlet, and a non-permeate gas outlet, the membrane comprising a separation layer supported by a porous support layer, the porous support layer comprising a polymeric material, the separation layer comprising a first polymide optionally blended with a second polymide, the first polymide being represented by formula (I): the second polyimide being represented by formula (II): where R 1 is a molecular segment selected from the group consisting of the molecular segments of formula (A), formula (B), formula (C), and combinations thereof: withdrawing a permeate gas comprising H 2 S from a permeate outlet of the membrane; and withdrawing a non-permeate gas from a non-permeate outlet of the membrane, wherein the non-permeate gas has a H 2 S concentration lower than that of the feed gas. 2 . The method of claim 1 , wherein 16% of the R 1 's are the molecular segment of formula (A), 64% of the R 1 's are the molecular segment of formula (B), and 20% of the R 1 's are the molecular segment of formula (C). 3 . The method of claim 1 , wherein the feed gas comprises 2 vol % to 20 vol % of H 2 S. 4 . The method of claim 1 , wherein the feed gas comprises 5-20 vol % of H 2 S. 5 . The method of claim 1 , wherein the feed gas is natural gas. 6 . The method of claim 1 , wherein the feed gas is natural gas comprising at least 500 ppm H 2 S and a balance of CO 2 and CH 4 . 7 . The method of claim 1 , wherein the feed gas is natural gas comprising at least 500 ppm H 2 S and a balance of CO 2 , CH 4 and N 2 . 8 . The method of claim 1 , wherein: 16% of the R 1 's are the molecular segment of formula (A), 64% of the R 1 's are the molecular segment of formula (B), and 20% of the R 1 's are the molecular segment of formula (C); and the feed gas comprises 500 ppm to 20 vol % of H 2 S. 9 . The method of claim 8 , wherein the feed gas is natural gas. 10 . The method of claim 8 , wherein the feed gas is natural gas comprising at least 500 ppm H 2 S and a balance of CO 2 and CH 4 . 11 . The method of claim 8 , wherein the feed gas is natural gas comprising at least 500 ppm H 2 S and a balance of CO 2 , CH 4 and N 2 . 12 . The method of claim 1 , wherein: 16% of the R 1 's are the molecular segment of formula (A), 64% of the R 1 's are the molecular segment of formula (B), and 20% of the R 1 's are the molecular segment of formula (C); and the feed gas is natural gas. 13 . The method of claim 1 , wherein: 16% of the R 1 's are the molecular segment of formula (A), 64% of the R 1 's are the molecular segment of formula (B), and 20% of the R 1 's are the molecular segment of formula (C); and the feed gas is natural gas comprising at least 500 ppm H 2 S and a balance of CO 2 and CH 4 . 14 . The method of claim 1 , wherein: 16% of the R 1 's are the molecular segment of formula (A), 64% of the R 1 's are the molecular segment of formula (B), and 20% of the R 1 's are the molecular segment of formula (C); and the feed gas is natural gas comprising at least 500 ppm H 2 S and a balance of CO 2 , CH 4 and N 2 . 15 . The method of claim 1 , wherein the feed gas is natural gas comprising 500 ppm of H 2 S. 16 . The method of claim 15 , wherein the feed gas is natural gas comprising at least 500 ppm H 2 S and a balance of CO 2 and CH 4 . 17 . The method of claim 15 , wherein the feed gas is natural gas comprising at least 500 ppm H 2 S and a balance of CO 2 , CH 4 and N 2 . 18 . The method of claim 1 , wherein the separation layer comprises the first polyimide but not the second polyimide. 19 . The method of claim 1 , wherein the separation layer comprises a blend of the first and second polyimides.
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Polyimides; Polyamide-imides; Polyester-imides; Polyamide acids or similar polyimide precursors · CPC title
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