Pervaporation membranes derived from polycyclo-olefinic block copolymers

Patent metadata

Field	Value
Publication number	US-10245562-B2
Application number	US-201514827624-A
Country	US
Kind code	B2
Filing date	Aug 17, 2015
Priority date	Aug 15, 2014
Publication date	Apr 2, 2019
Grant date	Apr 2, 2019

Abstract

A pervaporation membrane formed from a series of vinyl addition block polymers derived from functionalized norbornene monomers are disclosed and claimed. Also disclosed are the fabrication of membranes which exhibit unique separation properties, and their use in the separation of organic volatiles from biomass and/or organic waste, including butanol, phenol, and the like.

First claim

What is claimed is:

1. A pervaporation membrane comprising a block copolymer of the formula (VI):
(A) m - b -(B) n   (VI);

where each of m and n is an integer of at least 15;
b denotes a bond;
A and B are different from each other and independently selected from a repeat unit represented by formula (IVA), said repeat unit is derived from a monomer of formula (IV):

wherein:
denotes a place of bonding with another repeat unit;
p is an integer 0, 1 or 2;
R 3 , R 4 , R 5 and R 6 are the same or different and each independently of one another is selected from hydrogen, linear or branched (C 1 -C 16 )alkyl, hydroxy(C 1 -C 16 )alkyl, perfluoro(C 1 -C 12 )alkyl, (C 3 -C 12 )cycloalkyl, (C 6 -C 12 )bicycloalkyl, (C 7 -C 14 )tricycloalkyl, (C 6 -C 10 )aryl, (C 6 -C 10 )aryl(C 1 -C 3 )alkyl, perfluoro(C 6 -C 10 )aryl, perfluoro(C 6 -C 10 )aryl(C 1 -C 3 )alkyl, di(C 1 -C 2 )alkylmaleimide(C 3 -C 6 )alkyl, di(C 1 -C 2 )alkylmaleimide(C 2 -C 6 )alkoxy(C 1 -C 2 )alkyl, hydroxy, (C 1 -C 12 )alkoxy, (C 3 -C 12 )cycloalkoxy, (C 6 -C 12 )bicycloalkoxy, (C 7 -C 14 )tricycloalkoxy, (C 6 -C 10 )aryloxy(C 1 -C 3 )alkyl, (C 5 -C 10 )heteroaryloxy(C 1 -C 3 )alkyl, (C 6 -C 10 )aryloxy, (C 5 -C 10 )heteroaryloxy or (C 1 -C 6 )acyloxy, where each of the aforementioned substituents are optionally substituted with halogen or hydroxy.

2. The pervaporation membrane according to claim 1 wherein said polymer further comprises a third repeat unit forming a block terpolymer represented by formula (VII):
(A) m - b -(B) n - b -(C) o   (VII);

where m, n and b are as defined in claim 1 and o is an integer of at least 15;
C is same or different from A or B and independently selected from a repeat unit represented by formula (IVA), said repeat unit is derived from a monomer of formula (IV) as defined in claim 1 .

3. The pervaporation membrane according to claim 1 , wherein the copolymer is selected from the group consisting of:
a block copolymer derived from 5-hexylbicyclo[2.2.1]hept-2-ene and norbornenyl-2-trifluoromethyl-3,3,3-trifluoropropan-2-ol (HexNB-b-HFANB);
a block copolymer derived from 5-butylbicyclo[2.2.1]hept-2-ene and norbornenyl-2-trifluoromethyl-3,3,3-trifluoropropan-2-ol (BuNB-b-HFANB);
a block copolymer derived from 5-butylbicyclo[2.2.1]hept-2-ene and 1-(4-(bicyclo[2.2.1]hept-5-en-2-yl)butyl)-3,4-dimethyl-1H-pyrrole-2,5-dione (C 4 F 9 NB-b-BuDMMINB);
a block copolymer of derived from norbornenyl-2-trifluoromethyl-3,3,3-trifluoropropan-2-ol and 2-(bicyclo[2.2.1]kept-5-en-2-yl)bicyclo[2.2.1]heptane (HFANB-b-NBANB); and
a block copolymer of derived from 5-hexylbicyclo[2.2.1]hept-2-ene and 2-(bicyclo[2.2.1]hept-5-en-2-yl)bicyclo[2.2.1]heptane (HexNB-b-NBANB).

4. The pervaporation membrane according to claim 2 , wherein the terpolymer is selected from the group consisting of:
a block terpolymer derived from 5-butylbicyclo[2.2.1]hept-2-ene, norbornenyl-2-trifluoromethyl-3,3,3-trifluoropropan-2-ol and 5-butylbicyclo[2.2.1]hept-2-ene (BuNB-b-HFANB-b-BuNB); and
a block terpolymer derived from norbornenyl-2-trifluoromethyl-3,3,3-trifluoropropan-2-ol, 5-butylbicyclo[2.2.1]hept-2-ene, and norbornenyl-2-trifluoromethyl-3,3,3-trifluoropropan-2-ol (HFANB-b-BuNB-b-HFANB).

5. The pervaporation membrane according to claim 1 in a form of a tubular composite, hollow fiber, a dense film flat sheet, or a thin film composite.

6. The pervaporation membrane according to claim 1 , which is capable of preferential permeability to a volatile organic over water, said permeability increasing with increasing organic concentration of a feed stream.

7. The pervaporation membrane according to claim 6 , wherein said volatile organic comprises butanol.

8. The pervaporation membrane according to claim 6 , wherein said volatile organic comprises phenol.

9. The pervaporation membrane according to claim 7 having a flux for butanol of at least about 100 g/m 2 ·h from a fermentation broth comprising at least about 1% by weight butanol, wherein the flux for butanol is an amount of butanol (g) that flows through an unit area (m 2 ) of the pervaporation membrane per unit of time (h).

10. A method of separating an organic product from a feedstock selected from a fermentation broth or a waste containing the organic product comprising:
charging the feedstock to a pervaporation module containing a pervaporation membrane formed by a polymer according to claim 1 ; and
collecting a permeate vapor containing the organic product from the pervaporation module.

11. The method according to claim 10 , wherein the fermentation broth charged to the pervaporation module has a temperature from about 30° C. to about 110° C.

12. The method according to claim 10 , wherein a vacuum from about 0.1 in Hg to about 25 in Hg is applied to the pervaporation module.

13. The method according to claim 10 , wherein the pervaporation membrane is formed by a polymer selected from:
a block copolymer derived from 5-hexylbicyclo[2.2.1]hept-2-ene and norbornenyl-2-trifluoromethyl-3,3,3-trifluoropropan-2-ol (HexNB-b-HFANB);
a block copolymer derived from 5-butylbicyclo[2.2.1]hept-2-ene and norbornenyl-2-trifluoromethyl-3,3,3-trifluoropropan-2-ol (BuNB-b-HFANB);
a block copolymer derived from 5-butylbicyclo[2.2.1]hept-2-ene and 1-(4-(bicyclo[2.2.1]hept-5-en-2-yl)butyl)-3,4-dimethyl-1H-pyrrole-2,5-dione (C 4 F 9 NB-b-BuDMMINB);
a block copolymer of derived from norbornenyl-2-trifluoromethyl-3,3,3-trifluoropropan-2-ol and 2-(bicyclo[2.2.1]hept-5-en-2-yl)bicyclo[2.2.1]heptane (HFANB-b-NBANB); and
a block copolymer of derived from 5-hexylbicyclo[2.2.1]hept-2-ene and 2-(bicyclo[2.2.1]hept-5-en-2-yl)bicyclo[2.2.1]heptane (HexNB-b-NBANB).

14. The method according to claim 10 , wherein the pervaporation membrane is formed by a polymer selected from:
a block terpolymer derived from 5-butylbicyclo[2.2.1]hept-2-ene, norbornenyl-2-trifluoromethyl-3,3,3-trifluoropropan-2-ol and 5-butylbicyclo[2.2.1]hept-2-ene (BuNB-b-HFANB-b-BuNB); and
a block terpolymer derived from norbornenyl-2-trifluoromethyl-3,3,3-trifluoropropan-2-ol, 5-butylbicyclo[2.2.1]hept-2-ene, and norbornenyl-2-trifluoromethyl-3,3,3-trifluoropropan-2-ol (HFANB-b-BuNB-b-HFANB).

15. The method according to claim 10 , wherein the organic product is butanol, ethanol or phenol.

16. A method of separating butanol or phenol from a feedstock selected from a fermentation broth or a waste containing butanol or phenol comprising:
charging the feedstock to a pervaporation module containing a pervaporation membrane formed by a polymer selected from:
a block copolymer derived from 5-hexylbicyclo[2.2.1]hept-2-ene and norbornenyl-2-trifluoromethyl-3,3,3-trifluoropropan-2-ol (HexNB-b-HFANB);
a block copolymer derived from 5-butylbicyclo[2.2.1]hept-2-ene and norbornenyl-2-trifluoromethyl-3,3,3-trifluoropropan-2-ol (BuNB-b-HFANB);
a block copolymer derived from 5-butylbicyclo[2.2.1]hept-2-ene and 1-(4-(bicyclo[2.2.1]hept-5-en-2-yl)butyl)-3,4-dimethyl-1H-pyrrole-2,5-dione (C 4 F 9 NB-b-BuDMMINB);
a block copolymer of derived from norbornenyl-2-trifluoromethyl-3,3,3-trifluoropropan-2-ol and 2-(bicyclo[2.2.1]kept-5-en-2-yl)bicyclo[2.2.1]heptane (HFANB-b-NBANB);
a block copolymer of derived from 5-hexylbicyclo[2.2.1]hept-2-ene and 2-(bicyclo[2.2.1]hept-5-en-2-yl)bicyclo[2.2.1]heptane (HexNB-b-NBANB);
a block terpolymer derived from 5-butylbicyclo[2.2.1]hept-2-ene, norbornenyl-2-trifluoromethyl-3,3,3-trifluoropropan-2-ol and 5-butylbicyclo[2.2.1]hept-2-ene (BuNB-b-HFANB-b-BuNB); and

Assignees

• Promerus Llc
• Sumitomo Bakelite Co

Inventors

• Bell Andrew
• Burtovyy Oleksandr
• Takigawa Tamami

Classifications

• B01D2323/12

  Specific ratios of components used · CPC title

• B01D67/0002

  Organic membrane manufacture · CPC title

• B01D61/362

  Pervaporation · CPC title

• B01D69/087

  Details relating to the spinning process · CPC title

• B01D67/0095

  Drying · CPC title