Hybrid membrane separation systems

• US 4,944,882 A
• Filed: 04/21/1989
• Issued: 07/31/1990
• Est. Priority Date: 04/21/1989
• Status: Expired due to Fees

• Current Assignee: Bend Research Inc. (Lonza Group AG)
• Original Assignee: Bend Research Inc. (Lonza Group AG)
• Inventors: Ray, Roderick J., Newbold, David D.
• Primary Examiner(s): SEVER, FRANK
• Application Number:
  US07/341,646
• Time in Patent Office: 466 Days
• Field of Search: 210/641, 210/640, 210/634, 210/644-647, 210/649-655
• US Class Current: 210/640
• CPC Class Codes: B01D 61/025 Reverse osmosis; Hyperfiltration
• CPC Class Codes: B01D 61/027 Nanofiltration
• CPC Class Codes: B01D 61/362 Pervaporation
• CPC Class Codes: B01D 61/3621 comprising multiple pervaporation steps
• CPC Class Codes: B01D 61/364 Membrane distillation
• CPC Class Codes: B01D 61/58 Multistep processes

Abstract

Hybrid membrane-based separation systems are disclosed that are useful in separating solvents and solutes. The hybrid systems combine any of the solvent removal processes reverse osmosis, nanofiltration, membrane distillation and pervaporation with any one of more of the solute removal processes utilizing pervaporation membranes, supported-liquid membranes, coupled transport membranes, and membrane contactors, the solvent and solute removal processes forming part of a recycle stream that utilizes membrane separation retentates as feeds and as recycle feed stream make-up.

Claims

1. A method including a combination of membrane separations for the removal of solvent and solute from a process stream containing a solvent and at least one solute with less membrane surface area than would be required for the component membrane separations of said combination or with greater separation than that obtainable with the component membrane separations having the same membrane surface area, said method including a combination consisting essentially of the component membrane separations of

(a) providing a solvent removal process for selectively removing solvent from said process stream, said solvent removal process forming a solvent-rich portion and a solvent-poor portion and being selected from the membrane processes of reverse osmosis, nanofiltration, membrane distillation and pervaporation,

(b) providing at least one selective solute removal process for selectively removing solute from said process stream, said selective solute removal process forming a solute-rich portion and a solute-poor portion and being selected from the membrane processes of pervaporation, supported-liquid membranes, coupled transport, and membrane contactors, and

(c) providing said solvent removal process and said selective solute removal process as a part of a recycle stream having either of the following relationships:

(1) the solute-poor portion of the selective solute removal process comprises the feed for the solvent removal process and the solvent-poor portion of the solvent removal process is combined with the process stream to form the feed to the selective solute removal process;

or

(2) the solvent-poor portion of the solvent removal process comprises the feed for the selective solute removal process and the solute-poor portion of the selective solute removal process is combined with the process stream to form the feed to the solvent removal process.

2. The method of claim 1 wherein said solvent removal process is selected from the processes of reverse osmosis and nanofiltration.

3. The method of claim 2 wherein said selective solute removal processes is pervaporation.

4. The method of claim 2 wherein said selective solute removal process is supported-liquid membrane.

5. The method of claim 2 wherein said selective solute removal process is coupled transport.

6. The method of claim 2 wherein said selective solute removal process is membrane contactor.

7. The method of claim 2 wherein said selective solute removal process comprises supported-liquid membrane and pervaporation.

8. The method of claim 2 wherein said selective solute removal process comprises coupled transport and supported-liquid membrane.

9. The method of claim 2 wherein said selective solute removal process comprises coupled transport and pervaporation.

10. The method of claim 2 wherein said selective solute removal process comprises membrane contactor and pervaporation.

11. The method of claim 2 wherein said selective solute removal process comprises membrane contactor and supported-liquid membrane.

12. The method of claim 2 wherein said selective solute removal process comprises membrane contactor and coupled transport.

13. The method of claim 2 wherein said selective solute removal process comprises two supported-liquid membrane processes.

14. The method of claim 2 wherein said selective solute removal process comprises two coupled transport processes.

15. The method of claim 2 wherein said selective solute removal process comprises two membrane contactor processes.

16. The method of claim 1 wherein said solvent removal process is pervaporation.

17. The method of claim 16 wherein said selective solute removal process is pervaporation.

18. The method of claim 16 wherein said selective solute removal process is supported-liquid membrane.

19. The method of claim 16 wherein said selective solute removal process is membrane contactor.

20. The method of claim 1 wherein said solvent removal process is membrane distillation and said selective solute removal process is coupled transport.

21. The method of claim 1 wherein said solvent is water and said solvent removal process is reverse osmosis.

22. The method of claim 21 wherein said solute is phenol and said selective solute removal process is pervaporation.

23. The method of claim 21 wherein said solute comprises hops beta-acids and said selective solute removal process is supported-liquid membrane.

24. The method of claim 21 wherein said solute is chromium ion and said selective solute removal process is coupled transport.

25. The method of claim 21 wherein said solute is zinc ion and said selective solute removal process is membrane contactor.

26. The method of claim 21 wherein said solutes are citric acid and ethanol and said selective solute removal process comprises supported-liquid membrane and pervaporation.

27. The method of claim 21 wherein said solutes are dichromate ions and phenol and said selective solute removal process comprises coupled transport and supported-liquid membrane.

28. The method of claim 21 wherein said solutes are trichloroethane and chormium ion and said selective solute removal process comprises coupled transport and pervaporation.

29. The method of claim 21 wherein said solutes are ethanol and alpha-chymotripsin and said selective solute removal process comprises pervaporation and membrane contactor.

30. The method of claim 21 wherein said solutes are phenol and pyridine and said selective solute removal process comprises supported-liquid membrane and membrane contactor.

31. The method of claim 21 wherein said solutes are dichromate ions and phenol and said selective solute removal process comprises coupled transport and membrane contactor.

32. The method of claim 21 wherein said solutes are phenol and pyridine and said selective solute removal process comprises two supported-liquid membrane processes.

33. The method of claim 21 wherein said solutes are copper ion and chromium ion and said selective solute removal process comprises two coupled transport processes.

34. The method of claim 21 wherein said solutes are phenol and pyridine and said selective solute removal process comprises two membrane contactor processes.

35. The method of claim 1 wherein said solvent is water, said solvent removal process is pervaporation, said solute is ethanol, and said selective solute removal process is pervaporation.

36. The method of claim 1 wherein said solvent is water, said solvent removal process is pervaporation, said solute is citriic acid, and said selective solute removal process is supported-liquid membrane.

37. The method of claim 1 wherein said solvent is water, said solvent removal process is pervaporation, said solute is citric acid, and said selective solute removal process is membrane contactor.

38. The method of claim 1 wherein said solvent is water, said solvent removal process is membrane distillation, said solute is dichromate ion, and said selective solute removal process is coupled transport.