Immobilized-interface solute-transfer process

• US 4,997,569 A
• Filed: 02/06/1989
• Issued: 03/05/1991
• Est. Priority Date: 08/28/1984
• Status: Expired due to Term

• Current Assignee: The Trustees of The Stevens Institute of Technology (Stevens Institute Of Technology)
• Original Assignee: The Trustees of The Stevens Institute of Technology (Stevens Institute Of Technology)
• Inventors: Sirkar, Kamalesh K.
• Primary Examiner(s): SPEAR JR, FRANK
• Application Number:
  US07/308,958
• Time in Patent Office: 757 Days
• Field of Search: 210/637, 210/639, 210/644, 210/638, 210/640, 210/645, 210/648
• US Class Current: 210/637
• CPC Class Codes: B01D 11/0415 in combination with membranes
• CPC Class Codes: B01D 61/28 Apparatus therefor
• CPC Class Codes: B01D 61/32 Controlling or regulating

Abstract

In a process for transferring solute from a liquid feed solution to a liquid extractant which is substantially immiscible with the feed solution, one side of a porous membrane is contacted with the feed solution and the other side of the membrane with the extractant. One of the feed solution or the extractant preferentially wets the porous membrane. An interface-immobilizing pressure difference is maintained across the porous membrane in a direction and of a magnitude effective to oppose the tendency of the liquid which preferentially wets the membrane to flow through the membrane and disperse in the liquid on the opposite side. The interface between the feed solution and the extractant is thereby immobilized at the porous membrane.

Claims

1. A process for transferring solute from a liquid feed solution to a liquid extractant through a porous membrane, the feed solution and the extractant being substantially immiscible when in direct contact with each other, one of the feed solution and the extractant tending to preferentially wet the surface of the porous membrane to constitute a membrane-wetting liquid, the process comprising the steps of:

(a) contacting a first side of the porous membrane with the feed solution containing the solute;

(b) contacting a second side of the porous membrane with the liquid extractant so that the feed solution and the extractant can come into contact through the pores of the membranes; and

(c) maintaining an interface-immobilizing pressure difference between the feed solution on one side of the porous membrane and the extractant on the other side, the pressure difference being maintained in a direction across the membrane and in a pressure range effective to substantially prevent the membrane-wetting liquid from flowing through the membrane and dispersing in the fluid on the opposing side of the membrane, and thereby to immobilize the interface between the feed solution and the extractant at the porous membrane.

2. The process according to claim 1 in which the feed solution is an aqueous liquid and the extractant is substantially immiscible with water.

3. The process according to claim 2 in which the porous membrane is comprised of a hydrophilic material and the aqueous feed solution constitutes the membrane-wetting liquid, a pressure being maintained on the extractant and a pressure being maintained on the feed solution, the pressure on the extractant being greater than the pressure on the feed solution to oppose the passage of feed solution through the membrane.

4. The process according to claim 2 in which the feed solution is an aqueous fermentation broth and the solute is a fermentation product produced by fermentation of the broth, the fermentation product being soluble in the liquid extractant, the pores of the membrane being of a size substantially to prevent cellular debris in the fermentation broth from passing from the fermentation broth into the liquid extractant.

5. The process according to claim 4 further comprising the steps of:

(d) contacting a first side of a gas-permeable membrane with the fermentation broth; and

(e) contacting a second side of the gas-permeable membrane with an oxygen-containing gas so that oxygen can be introduced into the fermentation broth through the gas-permeable membrane and carbon dioxide can be withdrawn from the broth through the membrane.

6. The process according to claim 5 in which the fermentation produce is ethyl alcohol and the liquid extractant is selected from the group consisting of dibutyl phthalate and tributyl phosphate.

7. The process according to claim 1 in which the extractant is an aqueous liquid and the feed solution is substantially immiscible with water.

8. The process according to claim 7 in which the porous membrane is comprised of a hydrophobic material and the extractant liquid constitutes the membrane wetting fluid, a pressure being maintained on the extractant and a pressure being maintained on the aqueous feed solution, the pressure on the aqueous feed solution being greater than the pressure on the extractant to oppose the passage of extractant through the membrane.

9. The process according to claim 1 in which the feed solution is a first organic liquid and the extractant is a second organic liquid which is substantially immiscible with the first organic liquid.

10. The process according to claim 1 in which the step of contacting the first side of the porous membrane with the feed solution includes causing a stream of the feed solution to flow along the first side.

11. The process according to claim 10 in which the step of contacting the second side of the porous membrane with the extractant includes causing a stream of the extractant to flow along the second side.

12. The process according to claim 11 in which the stream of feed solution and the stream of extractant flow in generally opposing directions so that the transfer of solute from the stream of feed solution to the stream of extractant is a countercurrent process.

13. The process according to claim 1 further comprising the steps of:

(d) contacting a first side of an auxiliary porous membrane with the feed solution containing the solute;

(e) contacting a second side of the auxiliary porous membrane with an auxiliary liquid extractant so that the feed solution and the auxiliary extractant can come into contact through the pores of the membrane, the feed solution and the auxiliary extractant being substantially immiscible when in direct contact with each other; and

(f) maintaining a second interface-immobilizing pressure difference between the feed solution on one side of the auxiliary porous membrane and the auxiliary extractant on the other side, the second pressure difference being maintained in a direction across the membrane and in a pressure range effective to substantially prevent one of the feed solution and the auxiliary extractant which tends to preferentially wet the surface of the auxiliary porous membrane from flowing through the membrane and dispersing in the liquid on the opposing side of the membrane, and thereby to immobilize the interface between the feed solution and the auxiliary extractant at the auxiliary porous membrane.

14. A process for transferring solute from a liquid feed solution to a liquid back extractant by way of a liquid intermediate extractant, the feed solution and the intermediate extractant being substantially immiscible when in direct contact with each other and the intermediate extractant and the back extractant being substantially immiscible when in direct contact with each other, the process comprising the steps f:

(a) contacting a first side of an intermediate-extractant solute-transfer membrane with the feed solution containing the solute;

(b) contacting a second side of the intermediate-extractant solute-transfer membrane with the intermediate extractant so that the feed solution and the intermediate extractant can come into contact through the pores of the membrane;

(c) maintaining a first interface-immobilizing pressure difference between the feed solution on one side of the intermediate-extractant solute-transfer porous membrane and the intermediate extractant on the other side, the pressure difference being maintained in a direction across the membrane and in a pressure range effective to substantially prevent one of the feed solution and the intermediate extractant which tends to preferentially wet the surface of the intermediate extractant solute-transfer porous membrane from flowing through the membrane and dispersing in the liquid on the opposing side of the membrane and thereby to immobilize the interface between the feed solution and the intermediate extractant at the porous membrane;

(d) contacting a first side of a back-extractant solute-transfer membrane with the intermediate extractant;

(e) contacting a second side of the back-extractant solute-transfer porous membrane with the liquid back extractant so that the intermediate extractant and the back extractant can come into contact through the pores of the membrane; and

(f) maintaining a second interface-immobilizing pressure difference between the intermediate extractant on one side of the back-extractant solute-transfer porous membrane and the back extractant on the other side, the pressure difference being maintained in a direction across the membrane and in a pressure range effective to substantially prevent one of the intermediate extractant and the back extractant which tends to preferentially wet the surface of the back-extractant solute-transfer porous membrane from flowing through the membrane and dispersing in the liquid on the opposing side of the membrane, and thereby to immobilize the interface between the intermediate extractant and the back extractant at the back-extractant solute-transfer porous membrane.