Process for preparation of thin film composite membrane

• US 20060138043A1
• Filed: 12/23/2004
• Published: 06/29/2006
• Est. Priority Date: 12/23/2004
• Status: Abandoned Application

• Current Assignee: Council of Scientific & Industrial Research
• Original Assignee: Council of Scientific & Industrial Research
• Inventors: Kharul, Ulhas Kanhaiyalal, Lohokare, Harshada Ramesh, Achalpurkar, Manojkumar Prakash
• Application Number:
  US11/020,304
• Publication Number:
  US 20060138043A1
• Time in Patent Office: Days
• US Class Current: 210/490
• CPC Class Codes: B01D 53/228 characterised by specific membranes
• CPC Class Codes: B01D 69/125 In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction
• CPC Class Codes: B01D 71/70 Polymers having silicon in the main chain, with or without sulfur, nitrogen, oxygen or carbon only
• CPC Class Codes: B01D 71/701 Polydimethylsiloxane

Abstract

Thin Film Composite (TFC) membranes are prepared by coating a thin layer of aminated silicon rubber on the surface of highly porous substrate like ultrafiltration membrane, followed by crosslinking with reactive, aliphatic dialdehyde and curing at high temperature. The TFC membranes so prepared have amine functionality making them suitable for varied separation applications in gas separation, vapor permeation, pervaporation and other membrane separation processes.

Claims

1. A process for preparation of a thin film composite membrane based on aminated polysiloxanes, the process comprising coating a pretreated porous support membrane with a solution of aminated polysiloxane in an organic water immiscible solvent, partially drying the coated membrane and crosslinking the partially dried coated membrane with an aqueous solution of aliphaticdialdehyde to obtain a crosslinked membrane, heating the crosslinked membrane in controlled manner to obtain the thin film composite membrane.

2. A process as claimed in claim 1 wherein the porous support membrane is prepared from a polymer selected from the group consisting of polyacrylonitrile, polysulfone, polyethersulfones, polyetherimides, polyphenylene oxides, polyamides, polycarbonates, polyesters, polyethers, polyimides, polyamidimides and polyvinylidene fluoride.

3. A process as claimed in claim 1 wherein the porous support membrane is pretreated dipping in a solvent selected from the group consisting of alcohol, aliphatic or aromatic hydrocarbons and halogenated hydrocarbons, either only once or sequentially in series of solvents for 10 seconds to 48 hours.

4. A process as claimed in claim 1 wherein the porous support membrane is pretreated by drying in hot air flow or in an oven at 30°

C. to 100°

C.

5. A process as claimed in claim 1 wherein the aminated polysiloxane is selected from the group consisting of aminomethylpolysiloxane with amine value 5-90 mgKOH/gm, dimethyldiaminopolysiloxane with amine value 5-90 mgKOH/gm, poly(dimethylsiloxane)bis[[3-[(2-aminoethyl)amino]propyl]-dimethylsilyl] ether, poly(dimethylsiloxane)-co-(3-aminopropyl)-methylsiloxane, poly(di methylsiloxane)-bis-(3-aminopropyl)terminated, N-(2-Aminoethyl)-3-aminopropylmethyldimethoxysilane, N-(2-Aminoethyl)-3-aminopropyltri methoxysilane, 3-aminopropylmethyl-di-ethoxysilane, 3-aminopropyltri ethoxysilane, poly(dimethylsiloxane)-aminopropyl-dimethylterminated, aminofunctionalsiloxane copolymers containing aminomethyl, aminoethyl, aminopropylmethyl, aminobutyl;

aminoethylaminopropylmethylsiloxane-di methylsiloxane copolymers, aminoethylaminoisobutylmethylsiloxane-di methylsiloxane copolymers, and aminoethylaminopropylmethoxysiloxane-di methylsiloxane copolymers.

6. A process as claimed in claim 1 wherein the aminated polysiloxane solution is prepared in a water immiscible solvent selected from the group consisting of chlorinated solvents, aromatic or aliphatic hydrocarbons and water saturated higher alcohols.

7. A process as claimed in claim 1 wherein the concentration of the aminated polysiloxane is in the range of 0.2% to 50%.

8. A process as claimed in claim 1 wherein the aminated polysiloxane coated membrane is heated at 30°

C. to 100°

C. for 10 seconds to 6 hours by keeping in an oven or by drying with running hot air.

9. A process as claimed in claim 1 wherein the aminated polysiloxane coated on porous support membrane is crosslinked by dipping it into an aqueous dialdehyde solution for 2 seconds to 4 hours.

10. A process as claimed in claim 1 wherein the aliphatic dialdehyde has the following structure

Where R=_nH_m;

n=0-8;

m=0-16

11. A process as claimed in claim 1 wherein the dialdehyde treated membrane is heated at 30°

C. to 100°

C. for 10 seconds to 6 hours by keeping in an oven or by drying with running hot air.

12. A process as claimed in claim 1 wherein the concentration of aqueous dialdehyde solution used for crosslinking in interfacial manner is in the range of 0.1% v/v to 25% v/v.

13. A process as claimed in claim 1 wherein the aminated polysiloxane solution in appropriate solvent is coated on the surface of the porous support membrane by dip coating or spray coating.

14. A process as claimed in claim 1 wherein the porous support membrane is in the form of flat sheet, tubular or hollow fiber.

15. A process as claimed in claim 1 wherein the flat sheet porous support membrane is converted into a woven or non-woven fabric.

16. A process as claimed in claim 1 wherein the coating of aminated polysiloxane is effected on one side or on both sides of the porous support membrane or is impregnated inside pores of the porous support membrane.