Liquid Separations Using High Performance Mixed Matrix Membranes

• US 20080142440A1
• Filed: 12/18/2006
• Published: 06/19/2008
• Est. Priority Date: 12/18/2006
• Status: Abandoned Application

• Current Assignee: UOP Llc (Honeywell International Inc.)
• Original Assignee: UOP Llc (Honeywell International Inc.)
• Inventors: Lesch, David A., Tang, Man-Wing, Liu, Chunqing, Wilson, Stephen T.
• Application Number:
  US11/612,402
• Publication Number:
  US 20080142440A1
• Time in Patent Office: Days
• US Class Current: 210/640
• CPC Class Codes: B01D 53/228 characterised by specific membranes
• CPC Class Codes: B01D 61/362 Pervaporation
• CPC Class Codes: B01D 61/38 Liquid-membrane separation
• CPC Class Codes: B01D 67/0079 Manufacture of membranes comprising organic and inorganic components
• CPC Class Codes: B01D 67/00793 Dispersing a component, e.g. as particles or powder, in another component
• CPC Class Codes: B01D 69/141 Heterogeneous membranes, e.g. containing dispersed material; Mixed matrix membranes
• CPC Class Codes: B01D 69/14111 with nanoscale dispersed material, e.g. nanoparticles

Abstract

The present invention discloses a novel method of making high performance mixed matrix membranes (MMMs) using stabilized concentrated suspensions of solvents, uniformly dispersed polymer stabilized molecular sieves, and at least two different types of polymers as the continuous blend polymer matrix. MMMs as dense films or asymmetric flat sheet or hollow fiber membranes fabricated by the method described in the current invention exhibit significantly enhanced permeation performance for separations over the polymer membranes made from the continuous blend polymer matrix. MMMs of the present invention are suitable for a wide range of gas, vapor, and liquid separations such as alcohol/water, CO₂/CH₄, H₂/CH₄, O₂/N₂, CO₂/N₂, olefin/paraffin, iso/normal paraffins, and other light gases separations.

Claims

1. A process for separating at least one liquid from a mixture of liquids comprising:

a) providing a mixed matrix liquid separation membrane comprising a polymer stabilized molecular sieve approximately uniformly dispersed in a continuous polymer matrix phase comprising at least two different polymers wherein said continuous polymer matrix is permeable to at least one liquid in said mixture of liquids;

b) contacting the mixture of liquids on one side of the mixed matrix liquid separation membrane to cause said at least one liquid to permeate the mixed matrix liquid separation membrane; and

c) removing from a side opposite to said one side of the mixed matrix liquid separation membrane a permeate liquid composition comprising a portion of said at least one liquid which has permeated said mixed matrix liquid separation membrane.

2. The process of claim 1 wherein said process is a pervaporation process.

3. The process of claim 1 wherein at least one organic compound is removed from water.

4. The process of claim 3 wherein said organic compound is at least one compound selected from the group consisting of alcohols, phenols, chlorinated hydrocarbons, pyridines and ketones.

5. The process of claim 1 wherein sulfur-containing molecules are removed from gasoline or diesel fuels.

6. The process of claim 1 wherein said mixture of liquids comprises at least two different organic molecules.

7. The process of claim 6 wherein said at least two different organic molecules are selected from the group consisting of ethylacetate-ethanol, diethylether-ethanol, acetic acid-ethanol, benzene-ethanol, chloroform-ethanol, chloroform-methanol, acetone-isopropylether, allylalcohol-allylether, allylalcohol-cyclohexane, butanol-butylacetate, butanol-1-butylether,ethanol-ethylbutylether, propylacetate-propanol, isopropylether-isopropanol, methanol-ethanol-isopropanol, and ethylacetate-ethanol-acetic acid.

8. The process of claim 1 wherein said process increases product yield.

9. The process of claim 1 wherein said molecular sieves are selected from the group consisting of nano-molecular sieves, microporous molecular sieves, mesoporous molecular sieves, carbon molecular sieves and porous metal-organic frameworks.

10. The process of claim 1 wherein said polymer stabilized molecular sieves are stabilized by at least one polymer wherein said polymer is a hydroxyl or amino group-terminated polymer selected from the group consisting of polyethersulfones, sulfonated polyethersulfones, polyethers, polyether ketones, poly(ethylene imine)s, poly(amidoamine)s, and polyetherimides or is a hydroxyl group-containing glassy polymer selected from the group consisting of poly(vinyl alcohol)s, cellulose acetate, cellulose triacetate, cellulose acetate-butyrate, cellulose propionate, ethyl cellulose, methyl cellulose, nitrocellulose, and other cellulosic polymers.

11. The process of claim 1 wherein said at least two different polymers are selected from the group consisting of polysulfones, sulfonated polysulfones;

polyethersulfones, sulfonated polyethersulfones, polyethers, polyetherimides;

poly(styrenes);

styrene-containing copolymers selected from the group consisting of acrylonitrilestyrene copolymers, styrene-butadiene copolymers and styrene-vinylbenzylhalide copolymers;

polycarbonates;

cellulosic polymers selected from the group consisting of as cellulose acetate, cellulose triacetate, cellulose acetate-butyrate, cellulose propionate, ethyl cellulose, methyl cellulose, and nitrocellulose;

polyamides;

polyimides;

polyamide/imides;

polyketones, polyether ketones;

poly(arylene oxides);

poly(phenylene oxide) and poly(xylene oxide);

poly(esteramide-diisocyanate);

polyurethanes;

polyesters;

polysulfides;

poly(ethylene), poly(propylene), poly(butene-1), poly(4-methyl pentene-1), polyvinyls, e.g., poly(vinyl chloride), poly(vinyl fluoride), poly(vinylidene chloride), poly(vinylidene fluoride), poly(vinyl alcohol), poly(vinyl esters);

poly(vinyl acetate);

poly(vinyl propionate), poly(vinyl pyridines), poly(vinyl pyrrolidones), poly(vinyl ethers), poly(vinyl ketones), poly(vinyl aldehydes);

poly(vinyl formal);

poly(vinyl butyral);

poly(vinyl amides), poly(vinyl amines), poly(vinyl urethanes), poly(vinyl ureas), poly(vinyl phosphates), and poly(vinyl sulfates);

polyallyls;

poly(benzobenzimidazole);

polyhydrazides;

polyoxadiazoles;

polytriazoles;

poly (benzimidazole);

polycarbodiimides;

polyphosphazines;

microporous polymers;

interpolymers, block interpolymers containing repeating units from the above said polymers as terpolymers of acrylonitrile-vinyl bromide-sodium salt of para-sulfophenylmethallyl ethers; and

grafts and blends of said polymers.

12. The process of claim 1 wherein said at least two different polymers are selected from the group consisting of polysulfones, sulfonated polysulfones, polyethersulfones (PESs), sulfonated PESs, polyethers, polyetherimides, cellulosic polymers wherein said cellulosic polymers are cellulose acetate or cellulose triacetate,;

polyamides;

polyimides, poly(3,3′

,4,4′

-benzophenone tetracarboxylic dianhydride-pyromellitic dianhydride-3,3′

,5,5′

-tetramethyl-4,4′

-methylene dianiline) (poly(BTDA-PMDA-TMMDA)), poly(3,3′

,4,4′

-benzophenone tetracarboxylic dianhydride-pyromellitic dianhydride-4,4′

-oxydiphthalic anhydride-3,3′

,5,5′

-tetramethyl-4,4′

-methylene dianiline) (poly(BTDA-PMDA-ODPA-TMMDA)), poly(3,3′

,4,4′

-diphenylsulfone tetracarboxylic dianhydride-3,3′

,5,5′

-tetramethyl-4,4′

-methylene dianiline) (poly(DSDA-TMMDA)), poly(3,3′

,4,4′

-benzophenone tetracarboxylic dianhydride-3,3′

,5,5′

-tetramethyl-4,4′

-methylene dianiline) (poly(BTDA-TMMDA)), poly(3,3′

,4,4′

-diphenylsulfone tetracarboxylic dianhydride-pyromellitic dianhydride-3,3′

,5,5′

-tetramethyl-4,4′

-methylene dianiline) (poly(DSDA-PMDA-TMMDA)), poly[2,2′

-bis-(3,4-dicarboxyphenyl)hexafluoropropane dianhydride-1,3-phenylenediamine (poly(6FDA-m-PDA)), poly[2,2′

-bis-(3,4-dicarboxyphenyl)hexafluoropropane dianhydride-1,3-phenylenediamine-3,5-diaminobenzoic acid) (poly(6FDA-m-PDA-DABA)), P84 or P84HT;

polyamide/imides mixtures;

polyketones, polyether ketones; and

microporous polymers.

13. The process of claim 1 wherein said polymer in said polymer stabilized molecular sieve is the same as one of said at least two different polymers in said polymer matrix.

14. The process of claim 1 wherein said polymer in said polymer stabilized molecular sieve is different from either of said at least two different polymers in said polymer matrix.

15. The process of claim 1 wherein said mixed matrix membrane is a dense film mixed matrix membrane or an asymmetric flat sheet or hollow fiber mixed matrix membrane.

16. The process of claim 9 wherein said nano-molecular sieves comprise particles between 5 to 1000 nm in size wherein said nano-molecular sieves are selected from the group consisting of silicalite-1, SAPO-34, Si-MTW, Si-BEA, Si-MEL, LTA, FAU, Si-DDR, AlPO-14, AlPO-34, AlPO-18, SSZ-62, UZM-5, UZM-9, UZM-13, UZM-17, UZM-19, and MCM-65.

17. The process of claim 9 wherein said microporous molecular sieves are selected from the group consisting of zeolites and nonzeolites comprising aluminophosphates, silicoaluminophosphates, metalloaluminophosphates, elemental aluminophosphates, metallosilicoaluminophosphates and elemental silicoaluminophosphates.