Monolayer, composite, gas separation material, filter, gas separation device and method for manufacturing composite
US-12128366-B2 · Oct 29, 2024 · US
US2016184776A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016184776-A1 |
| Application number | US-201514725987-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 29, 2015 |
| Priority date | Dec 31, 2014 |
| Publication date | Jun 30, 2016 |
| Grant date | — |
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A carbon molecular sieve (CMS) membrane is made by pyrolyzing a polymeric precursor membrane in a pyrolysis atmosphere containing a sulfur-containing compound.
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What is claimed is: 1 . A method for producing a CMS membrane, comprising the steps of: forming a polymeric precursor membrane; and pyrolyzing the polymeric precursor membrane in a pyrolysis atmosphere containing 5 ppm (vol/vol) to 50% (vol/vol) of an sulfur-containing compound in a balance of inert gas. 2 . The method of claim 1 , wherein the sulfur-containing compound is selected from the group consisting of H 2 S, COS, CS 2 , SO 2 , and benzyl disulfide. 3 . The method of claim 1 , wherein the balance gas is N 2 , Ar or mixtures thereof. 4 . The method of claim 1 , wherein the polymeric precursor membrane comprises a separation layer, the separation layer comprising 6FDA:BPDA/DAM. 5 . The method of claim 1 , wherein the pyrolysis is conducted at a pressure of 0.25-1.0 bar (abs). 6 . The method of claim 1 , wherein the polymeric precursor membrane comprises a polyimide comprising alternating units of diamine-derived units and of dianhydride-derived units having the structure of formula I, wherein: each R 1 is a molecular segment independently selected from the group consisting of formula (A), formula (B), formula (C), and formula (D): Z is a molecular segment independently selected from the group consisting of formula (e), formula (f), formula (g), (h), (i), (j), and (k): the R 2 ′s are molecular segments independently selected from the group consisting of formula (i), formula (ii), formula (iii), formula (iv), formula (v), formula (vi), formula (vii), formula (viii), formula (ix), formula (x), formula (xi), formula (xii), formula (xiii), formula (xiv), formula (xv), formula (xvi) and formula (xvii): each X 5 is independently selected from the group consisting of hydrogen, —Cl, —OCH 3 , —OCH 2 CH 3 , and a straight or branched C 1 to C 6 alkyl group; R a is a straight or branched C 1 to C 6 alkyl group having a terminal carboxylic acid group; each Z′ is a molecular segment independently selected from the group consisting of the molecular segment of formula (xvii), formula (xviii), formula (xix), formula (xx), formula (xxi), formula (xxii), formula (xxiii), formula (xxiv), formula (xxv), formula (xxvi), formula (xxvii), formula (xxviii), formula (xxix), formula (xxxi), formula (xxxii), formula (xxxiii), formula (xxxiv), formula (xxxv), formula (xxxvi), formula (xxxvii), formula (xxxviii), formula (xxxix), and formula (xl): subscript p is an integer from 1-10; and each Z″ is a molecular segment independently selected from the group consisting of the molecular segment of formula (xxvii), formula (xxviii), and formula (xl). 7 . A CMS membrane produced according to the method of claim 1 . 8 . A method for separating a gas mixture, comprising the steps of feeding the gas mixture to the CMS membrane of claim 7 , withdrawing a permeate gas from a permeate outlet of the CMS membrane, and withdrawing a non-permeate gas from a non-permeate outlet of the CMS membrane that is deficient in at least one gas relative to the gas mixture.
characterised by specific membranes · CPC title
Chemical modification · CPC title
characterised by their properties · CPC title
Polymers having sulfur in the main chain, with or without nitrogen, oxygen or carbon only · CPC title
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