Process for methanol production

Claim 2

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.

Claim 3

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.

Claim 4

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

Claim 5

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

Claim 6

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

Claim 7

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.

Claim 8

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.

Claim 9

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.

Claim 10

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.

Claim 11

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.

Claim 12

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

Claim 13

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.

Claim 14

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.

Claim 15

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.

Claim 16

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

Claim 17

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

Claim 18

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.

Claim 19

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.

Claim 20

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

Claim 21

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

Claim 22

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.

Claim 23

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

Claim 24

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.

Claim 25

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.

Claim 26

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.

Claim 27

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.

Claim 28

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.

Claim 29

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.

Claim 30

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.

Claim 31

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.

Claim 32

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.

Claim 33

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.