Gas separations using high performance mixed matrix membranes

• US 7,998,246 B2
• Filed: 12/18/2006
• Issued: 08/16/2011
• Est. Priority Date: 12/18/2006
• Status: Expired due to Fees

• Current Assignee: UOP Llc (Honeywell International Inc.)
• Original Assignee: UOP Llc (Honeywell International Inc.)
• Inventors: Liu, Chunoing, Lesch, David A., Tang, Man-Wing, Wilson, Stephen T.
• Primary Examiner(s): Greene; Jason M
• Assistant Examiner(s): SHUMATE, ANTHONY R
• Application Number:
  US11/612,388
• Publication Number:
  US 20080141858A1
• Time in Patent Office: 1,702 Days
• Field of Search: 95/43, 95/45, 95/47, 96/4, 96/14
• US Class Current: 95/45
• CPC Class Codes: B01D 53/228 characterised by specific membranes
• CPC Class Codes: B01D 61/362 Pervaporation
• 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 69/1411 containing dispersed material in a continuous matrix
• 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 gas from a mixture of gases comprising:

a) providing a mixed matrix gas separation membrane comprising a polymer stabilized molecular sieves 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 gas in said mixture of gases wherein said polymer stabilized molecular sieves are stabilized by at least one polymer selected from the group consisting of polyethersulfones, sulfonated polyethersulfones, polyethers, polyether ketones, poly(ethylene imine)s, poly(amidoamine)s, polyetherimides cellulose acetate, cellulose triacetate, cellulose acetate-butyrate, cellulose propionate, ethyl cellulose, methyl cellulose, nitrocellulose, and then said polymer stabilized molecular sieves are dispersed in said continuous polymer matrix phase;

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

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

2. The process of claim 1 wherein said mixture of gases is selected from the group consisting of CO₂/CH₄, H₂/CH₄, H₂/N₂, O₂/N₂, CO₂/N₂, helium/methane, argon/ammonia, olefin/paraffin, and iso/normal paraffins.

3. The process of claim 1 wherein said mixture of gases comprises methane and at least one gas selected from the group consisting of carbon dioxide, oxygen, nitrogen, water vapor, hydrogen sulfide and helium.

4. The process of claim 1 wherein said mixture of gases comprises a mixture of air and volatile organic compounds.

5. 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.

6. 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), acrylonitrilestyrene copolymers, styrene-butadiene copolymers and styrene-vinylbenzylhalide copolymers;

polycarbonates, cellulose acetate, 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), poly(vinyl chloride), poly(vinyl fluoride), poly(vinylidene chloride), poly(vinylidene fluoride), 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; and

grafts and blends of said polymers.

7. 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, cellulose acetate, 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-MMDA)), 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));

polyamide/imides mixtures;

polyketones and polyether ketones.

8. 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.

9. 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.

10. 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.

11. The process of claim 5 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.

12. The process of claim 5 wherein said microporous molecular sieves are selected from the group consisting of zeolites, nonzeolitic aluminophosphates, nonzeolitic silicoaluminophosphates, nonzeolitic metalloaluminophosphates and nonzeolitic metallosilicoaluminophosphates.