Asymmetric polymeric membranes containing a metal-rich dense layer with a controlled thickness and method of making same
US-2017210101-A1 · Jul 27, 2017 · US
US10507437B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10507437-B2 |
| Application number | US-201715679159-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 17, 2017 |
| Priority date | Feb 27, 2015 |
| Publication date | Dec 17, 2019 |
| Grant date | Dec 17, 2019 |
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A gas separation membrane has a gas separation layer containing a cellulose resin, and an organopolysiloxane compound layer disposed on the gas separation layer in which Si ratio of the organopolysiloxane compound layer after immersion in chloroform to the organopolysiloxane compound layer before immersion in chloroform, the Si ratio being calculated by Mathematical expression (I), is 0.6 to 1.0. Si ratio=(Si—Kα X-ray intensity after immersion in chloroform)/(Si—Kα X-ray intensity before immersion in chloroform) Mathematical expression (I)
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What is claimed is: 1. A gas separation membrane comprising: a gas separation layer containing a cellulose resin; and an organopolysiloxane compound layer disposed on the gas separation layer, wherein a Si ratio of the organopolysiloxane compound layer after immersion in chloroform to the organopolysiloxane compound layer before immersion in chloroform, the Si ratio being calculated by Mathematical expression (I), is 0.6 to 1.0, Si ratio=(Si-Kα X-ray intensity after immersion in chloroform)/(Si-Kα X-ray intensity before immersion in chloroform), Mathematical expression (I) the organopolysiloxane compound layer has a structure in which organopolysiloxane compounds are linked to each other through a linking group selected from *—O-M-O—*, *—S-M-S—*, *—NR a C(═O)—*, *—NR b C(═O)NR b —*, *—O—CH 2 —O—*, *—S—CH 2 CH 2 —*, *—OC(═O)O—*, *—CH(OH)CH 2 OCO—*, *—CH(OH)CH 2 O—*, *—CH(OH)CH 2 S—*, *—CH(OH)CH 2 NR c —*, *—CH(CH 2 OH)CH 2 OCO—*, *—CH(CH 2 OH)CH 2 O—*, *—CH(CH 2 OH)CH 2 S—*, *—CH(CH 2 OH)CH 2 NR c —*, *—CH 2 CH 2 —*, *—C(═O)O − N + (R d ) 3 —*, *—SO 3 − N + (R e ) 3 —*, and *—PO 3 H − N + (R f ) 3 —*, where M represents a divalent to tetravalent metal atom; R a , R b , R c , R d , R e , and R f each independently represent a hydrogen atom or an alkyl group, the symbol * represents a linking site, the linking group *—CH 2 CH 2 —* is formed by a polymerization reaction of compounds having a vinyl group, and the organopolysiloxane compound layer contains 10 to 5,000 ppm of an organic solvent. 2. The gas separation membrane according to claim 1 , wherein the metal atom M is a metal atom selected from Be, Mg, Ca, Sc, Y, Ti, Zr, V, Cr, Mo, Mn, Fe, Co, Ni, Cu, Zn, B, Al, Ga, and In. 3. The gas separation membrane according to claim 1 , wherein the linking group is a linking group selected from *—O-M 1 -O—*, *—S-M 1 -S—*, *—O—CH 2 —O—*, *—S—CH 2 CH 2 —*, *—OC(═O)O 2 , *—CH 2 CH 2 —*, and *—C(═O)O − N + (R d ) 3 —*, where M 1 represents a metal atom selected from Zr, Fe, Zn, B, Al, and Ga; and R d represents a hydrogen atom or an alkyl group. 4. The gas separation membrane according to claim 3 , wherein the organopolysiloxane compound layer has a structure in which organopolysiloxane compounds are linked to each other through a linking group selected from *—O-M 1 -O—* and —S-M 1 -S—* and a structure in which organopolysiloxane compounds are linked to each other through a linking group selected from *—O—CH 2 —O—*, *—S—CH 2 CH 2 —*, *—OC(═O)O—*, *—CH 2 CH 2 —*, and *—C(═O)O − N + (R d ) 3 —*. 5. The gas separation membrane according to claim 1 , wherein the organopolysiloxane compound layer has at least one structure selected from (a) or (b): (a) a structure having a structure represented by General formula (1) and a structure represented by General formula (2) or General formula (3), or (b) a structure represented by General formula (4), where R represents an alkyl group or an aryl group; L A represents a single bond or a divalent linking group; X represents a linking group selected from *—O-M 1 -O—*, *—S-M-S—*, *—O—CH 2 —O—*, *—S—CH 2 CH 2 —*, *—OC(═O)O—*, *—CH 2 CH 2 —*, and *—C(═O)O − N + (R d ) 3 —* where M 1 represents Zr, Fe, Zn, B, Al, or Ga; R d represents a hydrogen atom or an alkyl group; m and n are each an integer of 2 or more; the symbol * represents a linking site; and the symbol ** represents a linking site in a siloxane bond. 6. The gas separation membrane according to claim 5 , wherein the structure of (a) further has a repeating unit represented by Formula (5), 7. The gas separation membrane according to claim 6 , wherein a content ratio of the repeating unit represented by Formula (5) in the organopolysiloxane compound layer is 0.01 to 0.55. 8. The gas separation membrane according to claim 1 , wherein the metal atom M is B or Al. 9. The gas separation membrane according to claim 3 , wherein the metal atom M 1 is B or Al. 10. The gas separation membrane according to claim 1 , wherein the cellulose resin contained in the gas separation layer is a cellulose resin having a repeating unit represented by Formula (A): where R 1 , R 2 , and R 3 each independently represent a group selected from a hydrogen atom, an alkyl group, and an acyl group. 11. The gas separation membrane according to claim 1 , wherein the gas separation membrane is an asymmetric membrane. 12. The gas separation membrane according to claim 11 , wherein the gas separation membrane has a thickness of 10 to 200 μm. 13. The gas separation membrane according to claim 11 , wherein the gas separation membrane is the asymmetric membrane supported by a nonwoven fabric. 14. The gas separation membrane according to claim 1 , wherein carbon dioxide is selectively permeated through the gas separation membrane to be separated from gas containing carbon dioxide and methane. 15. A gas separation module comprising the gas separation membrane according to claim 1 . 16. A gas separation apparatus comprising the gas separation module according to claim 15 . 17. A gas separation method comprising supplying gas to the gas separation membrane according to claim 1 . 18. The gas separation method according to claim 17 , wherein carbon dioxide is selectively permeated through the gas separation membrane to be separated from methane contained in the gas.
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