Solvent exchange drying of membranes for gas separation

• US 4,120,098 A
• Filed: 06/22/1976
• Issued: 10/17/1978
• Est. Priority Date: 06/22/1976
• Status: Expired due to Term

• Current Assignee: L'Air Liquide SA
• Original Assignee: E. I. du Pont de Nemours and Company (Corteva, Inc.)
• Inventors: Manos, Philip
• Primary Examiner(s): Spear, Jr., Frank A.
• Application Number:
  US05/698,695
• Time in Patent Office: 847 Days
• Field of Search: 210/500 M, 210/23 H, 210/321 R, 55/16, 264/41, 264/330, 264/340, 264/344, 34/9, 260/25 AY
• US Class Current: 34/337
• CPC Class Codes: B01D 67/0095 Drying

Abstract

Process for drying a water-wet permselective membrane by contacting the membrane with water replacement liquid under conditions which result in minimal shrinkage based on the surface tension, viscosity, concentration, molar volume, and temperature of the components of the system.

Claims

1. In the process for drying a semipermeable, polymeric membrane that is wet with an aqueous membrane-wetting liquid by contacting the wet membrane with at least one replacement liquid inert to the membrane and to the membrane-wetting liquid to remove water from the membrane and removing the replacement liquid from the membrane;

the improvement which comprises contacting, at a temperature of about from -50°

C. to 50°

C., said wet semipermeable polymeric membrane in which the polymer has a Critical Surface Tension of at least about 42 dynes per centimeter with at least one replacement liquid consisting essentially of at least one organic solvent which is selected from the class consisting of an aliphatic alcohol having 1-3 carbon atoms, acetonitrile, and an aqueous solution thereof, and in which the organic solvent is capable of penetrating the membrane and has a surface tension of less than about 35 dynes per centimeter at 20°

C., and a hydrogen bonding parameter of at least about 1.5 (calories per cubic centimeter)^1/2, and wherein the relative surface tension of the membrane wetting liquid, the concentration of the solvent in the replacement liquid and the viscosity and the molar volume of the organic solvent are such as to provide a Permeation Factor less than or equal to about 50, provided, however, that when the temperature of contact is about from 20°

C. to -50°

C., the Permeation Factor is less than or equal to about 100 - 2.5 T, wherein T is the temperature of contact in degrees centigrade; and

after water has been substantially completely removed from the membrane, evaporating the replacement liquid to obtain a membrane free of water and replacement liquid.

2. A process of claim 1 wherein the Permeation Factor is less than about 30 for each step in which the water-wet membrane is contacted with replacement liquid.

3. A process of claim 1 wherein the first replacement liquid with which the water-wet membrane is contacted consists essentially of substantially anhydrous organic solvent.

4. A process of claim 1 wherein the first replacement liquid with which the water-wet membrane is contacted consists essentially of an aqueous solution of organic solvent.

5. A process of claim 4 wherein the organic solvent is selected from methanol, ethanol and isopropanol.

6. A process of claim 4 wherein the concentration of the organic solvent in the replacement liquid is continuously increased to substantially 100%.