# US 2014/0360366 A1 · Azide crosslinked and physically crosslinked polymers for membrane separation

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- Number: US 2014/0360366 A1
- Document ID: US20140360366A1
- Status: Published application
- Kind: A1
- Application number: 14/345,343
- Filed: 2012-09-20
- Published: 2014-12-11
- Earliest claimed: 2011-09-21
- Assignees: Dow Global Technologies LLC
- Applicants: Dow Global Technologies
- Inventors: Scott T. Matteucci; Clark H. Cummins; William J. Kruper; Harry Craig Silvis
- Web page: https://patentgrep.com/patent/US20140360366A1

## CPC

- B01D 71/58: Other polymers having nitrogen in the main chain, with or without oxygen or carbon only
- B01D 53/22: by diffusion (manufacturing semi-permeable membranes B01D67/00; form, structure or properties of semi-permeable membranes B01D69/00; material for semi-permeable membranes B01D71/00)
- C08K 5/28: Azides
- C08K 5/43: Compounds containing sulfur bound to nitrogen
- B01D 2053/221: {Devices}
- B01D 2257/504: Carbon dioxide
- B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28)
- C08K: Use of inorganic or non-macromolecular organic substances as compounding ingredients (paints, inks, varnishes, dyes, polishes, adhesives C09)

## Abstract

The present invention appreciates that compounds comprising ester linkages and nitrogen-containing moieties that are at least divalent (e.g., urea, urethane, amide, etc.) can be crosslinked with azides to form membranes that are resistant to C02 plasticization, that are selective for acid gases relative to nonpolar gases such as hydrocarbons, and that have high acid gas flux characteristics. The resultant membranes have stable structure and stable separation properties at higher temperatures and pressures. The membranes are compatible with many industrial processes in which polar gases are separated from nopolar gases. In an exemplary mode of practice, the membranes can be used to separate acid gases from the hydrocarbon gases in natural or non-acid gas components of flue gas mixtures (e.g., N2, O2, etc.).

## Claims

### Claim 1

A physically and chemically cured membrane composition comprising an inlet face and an outlet face, and incorporating ingredients comprising:
a) at least one membrane compound comprising a plurality of ester moieties and a plurality of N-containing backbone moieties, wherein each N-containing moiety is at least divalent, wherein the at least one compound comprises ester repeat units of Formula I:
and at least one second repeat unit selected from the esteramide units of Formula II and/or the esteramide units of Formula III, and optionally at least one repeat unit of the ester-urethane units of Formula IV:
wherein:
each R is independently selected from a C2-C20 non-aromatic hydrocarbylene group, a C2-C20 non-aromatic heterohydrocarbylene group, or a polyalkylene oxide group having a group molecular weight of from about 100 to about 5000 g/mol;
each R1 independently is a bond or a C1-C20 non-aromatic hydrocarbylene group;
each R2 independently a C1-C20 non-aromatic hydrocarbylene group;
each RN independently is —N(R3)—Ra—N(R3)—, where each R3 is independently H or a C1-C6 alkyl or RN is a C2-C20 heterocycloalkylene group containing at least two nitrogen atoms;
w+x+y+z=1, 0<w<1, and at least one of x and y is greater than 0;
Ra is a C2-C20 non-aromatic hydrocarbylene group; and
n is at least 1 and has a mean value less than 2;
and
b) at least one azide crosslinking agent that chemically crosslinks the at least one membrane compound.

### Claim 2 (depends on 1)

The composition according to claim 1, wherein the at least one compound has a number average molecular weight in the range from 2000 to 50,000.

### Claim 3 (depends on 1)

The composition according to claim 1, wherein the at least one compound is nonaromatic.

### Claim 4 (depends on 1)

The composition according to claim 1, wherein a repeating unit according to Formula I has a structure according to Formula V and a repeating unit according to Formula II has the structure according to Formula VI:
wherein q and r are 4, n is 2, p is 5, x is 0.18 and y is 0.82.

### Claim 5 (depends on 1)

The composition according to claim 1, wherein the azide crosslinking agent comprises a compound represented by the following formula
(N3)m—R10
wherein m is 1 to 6 and R10 is an m-valent moiety that may be aryl or nonaryl; saturated or unsaturated; linear or branched or cyclic; and/or substituted or unsubstituted.

### Claim 6 (depends on 1)

The composition according claim 1, wherein the azide crosslinking agent comprises a compound represented by the following formula
wherein each Ro and R11 independently is a divalent linking group that may comprise a heteroatom such as one or more of O, S, P, or the like and that may be linear, branched, cyclic, polycyclic, fused ring, or the like; with the proviso that each Ro independently may be a single bond.

### Claim 7 (depends on 6)

The composition according to claim 6, wherein R11 is a linear, branched, cyclic, or polycyclic hydrocarbyl moiety of the formula
wherein v is 1 to 10; each R12 independently is H, alkyl of 1 to 10 carbon atoms, alkoxy of 1 to 10 carbon atoms.

### Claim 8 (depends on 6)

The composition according to claim 6, wherein each of Ro and R11 independently is a linear, branched, cyclic, or polycyclic alkoxylene moiety of the formula
—(OR13)q—
wherein q is 1 to 10; and R13 is a divalent alkylene moiety that may be linear, branched, cyclic, or polycyclic.

### Claim 9 (depends on 6)

The composition according to claim 6, wherein each Ro and R11 independently is selected from oxygen,

### Claim 10 (depends on 1)

The composition according to claim 1, wherein the azide crosslinking agent comprises a compound having a fused ring structure.

### Claim 11 (depends on 1)

The composition according to claim 1, wherein the azide crosslinking agent comprises a substituted or unsubstituted material according to the formula

### Claim 12 (depends on 1)

The composition according to claim 1, wherein the azide crosslinking agent comprises a substituted or unsubstituted material according to the formula

### Claim 13 (depends on 1)

The composition according to claim 1, wherein the azide crosslinking agent comprises a substituted or unsubstituted material according to the formula N3—(R13O)q—Ro—N3, wherein R0 is selected from oxygen,
R13 is a divalent alkylene moiety that may be linear, branched, cyclic, or polycyclic, and q is 1 to 10.

### Claim 15 (depends on 1)

A method of making a separation system, comprising the steps of:
(a) providing a separation membrane derived from ingredients comprising at least one membrane compound comprising a plurality of ester moieties and a plurality of N-containing, divalent backbone moieties according to claim 1 and at least one azide crosslinking agent according to claim 1;
(b) causing the membrane to be used to separate components of a feed mixture to provide a first separation product that is enriched with respect to an ingredient of the feed mixture and a second separation product that is depleted with respect to the feed ingredient.

### Claim 16 (depends on 1)

A purification system comprising:
(a) a feed mixture comprising at least one acid gas and at least one nonpolar gas;
(b) a membrane having an inlet face and an outlet face, wherein the membrane is derived from ingredients comprising at least one compound comprising a plurality of ester moities and a plurality of N-containing, divalent backbone moieties and at least one azide crosslinking agent according to claim 1; and
(c) a pressure differential between the inlet face and the outlet face effective to provide a first separation product that is enriched with respect to the acid gas relative to the feed mixture and a second separation product that is depleted with respect to the acid gas relative to the feed mixture when the feed mixture is caused to contact the membrane.
