Process for methanol production

• US 4,181,675 A
• Filed: 09/19/1978
• Issued: 01/01/1980
• Est. Priority Date: 09/19/1978
• Status: Expired due to Term

• Current Assignee: Permea Incorporated
• Original Assignee: Monsanto Company (Bayer AG)
• Inventors: Makin, Earle C., Okamoto, K. Keith
• Primary Examiner(s): Mars, Howard T.
• Application Number:
  US05/943,841
• Time in Patent Office: 469 Days
• Field of Search: 260/449.5, 55/16, 55/158, 48/DIG. 5
• US Class Current: 518/705
• CPC Class Codes: B01D 53/22 by diffusion manufacturing semi-permeable membranes B01D67/00; form, structure or properties of semi-permeable membranes B01D69/00; material for semi-permeable membranes B01D71/00
• CPC Class Codes: C07C 29/1512 characterised by reaction conditions
• CPC Class Codes: C07C 29/1516 Multisteps
• CPC Class Codes: C07C 31/04 Methanol
• CPC Class Codes: Y02P 20/129 Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
• CPC Class Codes: Y02P 20/50 Improvements relating to the production of bulk chemicals
• CPC Class Codes: Y02P 20/584 Recycling of catalysts
• CPC Class Codes: Y10S 48/05 Diffusion membrane for gas reaction or separation

Abstract

An improved methanol synthesis process is provided wherein synthesis gas containing hydrogen and carbon dioxide is passed over a methanol synthesis catalyst, cooled to condense methanol and water in the reacted gas, the liquids separated, a purge gas stream removed while the remaining reacted gas is recycled to the synthesis catalyst, the purge gas separated by contacting the outer surfaces of a plurality of hollow fiber membranes selectively permeable to hydrogen and carbon dioxide to form a permeant gas depleted in hydrogen and carbon dioxide and a permeate gas enriched in said gases and the enriched permeate gas is combined with the synthesis gas. In an optional embodiment, methanol vapor is first recovered from the purge gas prior to contacting the selectively permeable membranes, preferably by a water scrub.

Claims

1. In a methanol synthesis process wherein methanol is synthesized from a synthesis gas comprising hydrogen and carbon dioxide by passing said synthesis gas over a methanol synthesis catalyst at methanol-forming conditions to form a gaseous mixture including methanol, water and unreacted carbon dioxide, said gaseous mixture is cooled, methanol and water are condensed therefrom and separated from the uncondensed gaseous mixture, a portion of said uncondensed gaseous mixture is removed as purge gas and the remaining uncondensed gaseous mixture is recycled to contact said methanol synthesis catalyst, the improvement comprising contacting said purge gas with the outside surfaces of a plurality of hollow fiber membranes selectively permeable to both hydrogen and carbon dioxide to form a permeant gas stream depleted in hydrogen and carbon dioxide and a permeate gas stream enriched in both said gases, and combining said enriched permeate gas stream with said synthesis gas.

2. The process of claim 1 wherein said removed purge gas is treated to recover methanol vapor therein prior to contacting said purge gas with said membranes.

3. The process of claim 2 wherein said methanol vapor is absorbed in a water scrub.

4. The process of claim 3 wherein said absorbed methanol is recovered by distillation.

5. The process of claim 1 wherein carbon dioxide gas is added to said enriched permeate gas stream.

6. The process of claim 5 wherein said carbon dioxide gas is added in an amount substantially equivalent to the stoichiometric excess of hydrogen over carbon oxides in said enriched permeate gas stream.

7. The process of claim 1 wherein a pressure differential of from about 3 to about 100 atmospheres is maintained between said purge gas and said permeate gas stream.

8. The process of claim 7 wherein said permeate gas stream is maintained at a pressure of at least about 25 atmospheres and combined with said synthesis gas at substantially the same pressure.

9. The process of claim 1 wherein said hollow fiber membranes have outside diameters of from about 150 to about 800 microns and a wall thickness of about 50 to about 300 microns.

10. The process of claim 1 wherein said membranes are multicomponent hollow fiber membranes which comprise a porous hollow fiber separation membrane and a coating in occluding contact with the outside surface thereof.

11. The process of claim 10 wherein said separation membrane comprises polysulfone and said coating comprises poly(siloxane).

27. The process of claim 1 wherein said enriched permeate gas stream is combined with said synthesis gas before final compression of said synthesis gas to methanol synthesis pressure.

12. In a methanol synthesis process wherein methanol is synthesized from a synthesis gas comprising hydrogen and carbon dioxide by passing said synthesis gas over a methanol synthesis catalyst at methanol-forming conditions to form a gaseous mixture including methanol, water and unreacted carbon dioxide, said gaseous mixture is cooled, methanol and water are condensed therefrom and separated from the uncondensed gaseous mixture, a portion of said uncondensed gaseous mixture is removed as purge gas and the remaining uncondensed gaseous mixture is recycled to contact said methanol synthesis catalyst, the improvement comprising contacting said purge gas with the outside surfaces of a plurality of hollow fiber membranes selectively permeable to both hydrogen and carbon dioxide and having an outside diameter of from about 150 to 800 microns and a wall thickness of from about 50 to 300 microns to form a permeant gas stream depleted in hydrogen and carbon dioxide and a permeate gas stream enriched in both said gases, and combining said enriched permeate gas stream with said synthesis gas.

13. The process of claim 12 wherein said removed purge gas is treated to recover methanol vapor therein prior to contacting said purge gas with said membranes.

14. The process of claim 13 wherein said methanol vapor is absorbed in a water scrub and recovered by distillation.

15. The process of claim 12 wherein carbon dioxide gas is added to the enriched permeate gas stream.

16. The process of claim 15 wherein said carbon dioxide gas is added in an amount substantially equivalent to the stoichiometric excess of hydrogen over carbon oxides in said permeate gas stream.

17. The process of claim 12 wherein a differential in pressure of from about 3 to about 100 atmospheres is maintained between said purge gas and said permeate gas stream.

18. The process of claim 12 wherein said purge gas is maintained at a pressure of from about 30 to about 100 atmospheres.

19. The process of claim 12 wherein said permeate gas stream is maintained at a pressure of from about 10 to about 30 atmospheres.

20. The process of claim 12 wherein said membranes are multicomponent hollow fiber membranes which comprise a porous hollow fiber separation membrane and a coating in occluding contact with the outside surface thereof.

21. The process of claim 20 wherein said porous separation membrane comprises polysulfone and said coating comprises poly(siloxane).

22. The process of claim 20 wherein said porous separation membrane comprises polysulfone having a molecular weight of at least about 10,000 and said coating comprises poly(siloxane) cross-linked to provide a silicone rubber.

28. The process of claim 12 wherein said enriched permeate gas stream is combined with said synthesis gas before final compression of said synthesis gas to methanol synthesis pressure.

23. In a methanol synthesis process wherein methanol is synthesized from a synthesis gas comprising hydrogen and carbon dioxide by passing said synthesis gas over a methanol synthesis catalyst at methanol-forming conditions to form a gaseous mixture including methanol, water and unreacted carbon dioxide, said gaseous mixture is cooled, methanol and water are condensed therefrom and separated from the uncondensed gaseous mixture, a portion of said uncondensed gaseous mixture is removed as purge gas and the remaining uncondensed gaseous mixture is recycled to contact said methanol synthesis catalyst, the improvement comprising contacting said purge gas with the outside surfaces of a plurality of hollow fiber membranes selectively permeable to both hydrogen and carbon dioxide and having an outside diameter of from about 150 to 800 microns and a wall thickness of from about 50 to 300 microns to form a permeant gas stream depleted in hydrogen and carbon dioxide and a permeate gas stream enriched in both said gases, adding carbon dioxide gas to the enriched permeate gas stream, and combining said enriched permeate gas stream with said synthesis gas.

24. The process of claim 23 wherein said carbon dioxide gas is added to the enriched permeate gas stream in an amount substantially equivalent to the stoichiometric excess of hydrogen over carbon oxides in said permeate gas stream.

25. The process of claim 23 wherein said membranes are multicomponent hollow fiber membranes which comprise a porous hollow fiber separation membrane and a coating in occluding contact with the outside surface thereof.

26. The process of claim 25 wherein said porous separation membrane comprises polysulfone and said coating comprises poly(siloxane) cross-linked to provide a silicone rubber.

29. The process of claim 23 wherein said enriched permeate gas stream is combined with said synthesis gas before final compression of said synthesis gas to methanol synthesis pressure.

30. The process of claim 23 wherein methanol vapor in said purge gas is absorbed in a water scrub prior to contacting said purge gas with said membranes.