Membrane drying process and system

Claim 2

A membrane process for the enhanced purification of a feed gas stream comprising: (a) passing a feed gas stream containing an impurity to be separated therefrom to a permeable membrane system capable of selectively permeating said impurity, said impurity having a separation factor in said system of at least about 15 with respect to said feed stream and/or the components thereof, said membrane system comprising a composite membrane or an asymmetric membrane having a substrate or less dense region porosity greater than about 0.05% to achieve a significant degree of radial mixing across said substrate portion of the membrane; (b) providing means on the outer side of said membrane to establish a countercurrent flow pattern across the permeate and non-permeate surfaces of the membrane comprising said substrate portion and a skin or separation layer portion thereof, said membrane system comprising hollow fiber membranes arranged so as to achieve an essentially uniform flow of gas across both feed and permeate sides of the membrane comprising said substrate portion and a skin or separation layer portion thereof; (c) passing purge gas on the permeate side of the membrane, said purge gas facilitating the permeation and removal of said impurity through the membrane, said purge gas being employed at a cleaning ratio of at least about 0.5, said cleaning ratio being the ratio of the STP volumetric purge gas flow rate to the STP volumetric non-permeate product flow rate divided by the ratio of the pressure on the low pressure, permeate side of the membrane to the pressure on the high pressure, feed side of the membrane; (d) removing non-permeate gas from the membrane system as desired product gas, said non-permeate gas comprising said feed gas stream with essentially all of the impurity removed therefrom, with negligible loss of said feed gas stream as a result of permeation thereof through the membrane; and (e) separately removing purge gas and said permeate gas from the membrane system, said permeate gas comprising essentially all of the impurity to be separated from the feed gas stream, whereby the desired purification is enhanced, with high recovery of the non-permeate product gas, the membrane system exhibiting a significant degree of countercurrency of performance, with the purge gas substituting for co-permeation of desired product gas in facilitating the permeation of the impurity and its removal from the surface of the membrane, thus maintaining the driving force for the passage of the impurity across said membrane.

Claim 3

The process of claim 1 in which said cleaning ratio is from about 0.6 to about 1.7.

Claim 4

The process of claim 2 in which said cleaning ratio is greater than unity.

Claim 5

The process of claim 1 in which said impurity has a separation factor of greater than about 100 with respect to said feed stream.

Claim 6

The process of claim 4 in which said impurity has a separation factor of greater than about 1,000 with respect to said feed stream and the components thereof.

Claim 7

The process of claim 1 in which said feed gas comprises air, said impurity being water and said purification comprising air drying.

Claim 8

The process of claim 6 in which said water has a separation factor of greater than 1,000 with respect to feed air and the oxygen and nitrogen components thereof.

Claim 9

The process of claim 7 in which said cleaning ratio is greater than unity, said water being nearly completely removed from said product air.

Claim 10

The process of claim 8 in which said hollow fibers are helically wound, with the active length thereof being essentially uniform, thus enabling said uniform flow of gas across the membrane surface to be facilitated.

Claim 11

The process of claim 8 in which said means to establish a countercurrent flow pattern across the surfaces of the membrane comprises an impervious barrier that encases the membrane along the longitudinal outer surface thereof.

Claim 12

The process of claim 1 in which said substrate porosity is greater than 0.5%.

Claim 13

The process of claim 11 in which said substrate porosity is from about 0.5% to about 5% or more.

Claim 14

The process of claim 1 in which said feed gas comprises air, said impurity comprises water, said purge gas is essentially dry, the cleaning ratio being greater than unity, said hollow fibers being helically wound with the active length thereof being essentially uniform, said hollow fibers being encased in an impervious barrier along the longitudinal outer surface thereof.

Claim 15

The process of claim 13 in which said substrate porosity is greater than 0.5%.

Claim 16

The process of claim 14 in which said substrate porosity is from about 0.5% to about 5% or more.

Claim 17

A membrane system for the enhanced purification of a feed gas stream comprising: (a) conduit means for passing a feed gas stream containing an impurity to be separated therefrom to a permeable membrane system; (b) a permeable membrane system adapted to receive said feed gas, said system being capable of selectively permeating said impurity, the material of said membrane system being such that the impurity has a separation factor of at least about 15 with respect to said feed gas and/or the components thereof, said membrane system comprising a composite membrane or an asymmetric membrane having a substrate or less dense region porosity greater than about 0.05% to achieve a significant degree of radial mixing across the substrate portion of the membrane, said composite or asymmetric membrane comprising hollow fiber membranes arranged so as to achieve an essentially uniform flow of gas across the membrane comprising said substrate portion and a skin or separation layer portion thereof; (c) means on the outer side of said membrane to establish a countercurrent flow pattern across the permeate and non-permeate surface of the membrane comprising said substrate portion and a skin or separation layer portion thereof; (d) conduit means for providing purge gas on the permeate side of the membrane, such as to provide a cleaning ratio of at least about 0.5, said cleaning ratio being the ratio of the STP volumetric purge gas flow rate to the STP volumetric non-permeate product flow rate divided by the ratio of the pressure on the low pressure, permeate side of the membrane to the pressure on the high pressure, feed side of the membrane; (e) means for removing non-permeate gas from the membrane system as desired product gas, said non-permeate gas comprising said feed gas stream with essentially all of the impurity removed therefrom, with negligible loss of said feed gas stream as a result of permeation thereof through the membrane; and (f) separate means for removing purge gas and said permeate gas from the membrane system said permeate gas comprising essentially all of the impurity to be separated from the feed gas stream, whereby the membrane system serves to enhance the desired purification, with high recovery of the non-permeate product gas, the membrane system exhibiting a significant degree of countercurrency of performance, with the purge gas substituting for co-permeation of desired product gas in facilitating the permeation of the impurity and its removal from the surface of the membrane, thus maintaining the driving force for the passage of the impurity across the membrane.

Claim 18

A membrane system for the enhanced purification of a feed gas stream comprising: (a) conduit means for passing a feed gas stream containing an impurity to be separated therefrom to a permeable membrane system; (b) a permeable membrane system adapted to receive said feed gas, said system being capable of selectively permeating said impurity, the material of said membrane system being such that the impurity has a separation factor of at least about 15 with respect to said feed gas and/or the components thereof, said membrane system comprising a composite membrane or an asymmetric membrane having a substrate or less dense region porosity greater than about 0.05% to achieve a significant degree of radial mixing across the substrate portion of the membrane, said composite or asymmetric membrane comprising hollow fiber membranes arranged so as to achieve an essentially uniform flow of gas across the membrane comprising said substrate portion and a skin or separation layer portion thereof; (c) means on the outer side of said membrane to establish a countercurrent flow pattern across the permeate and non-permeate surface of the membrane comprising said substrate portion and a skin or separation layer portion thereof; (d) conduit means for providing purge gas on the permeate side of the membrane, such as to provide a cleaning ratio of at least about 0.5, said cleaning ratio being the ratio of the STP volumetric purge gas flow rate to the STP volumetric non-permeate product flow rate divided by the ratio of the pressure on the low pressure, permeate side of the membrane to the pressure on the high pressure, feed side of the membrane; (e) means for removing non-permeate gas from the membrane system as desired product gas, said non-permeate gas comprising said feed gas stream with essentially all of the impurity removed therefrom, with negligible loss of said feed gas stream as a result of permeation thereof through the membrane; and (f) separate means for removing purge gas and said permeate gas from the membrane system said permeate gas comprising essentially all of the impurity to be separated from the feed gas stream, whereby the membrane system serves to enhance the desired purification, with high recovery of the non-permeate product gas, the membrane system exhibiting a significant degree of countercurrency of performance, with the purge gas substituting for co-permeation of desired product gas in facilitating the permeation of the impurity and its removal from the surface of the membrane, thus maintaining the driving force for the passage of the impurity across the membrane.

Claim 19

The membrane system of claim 16 in which said membrane material is such that the impurity has a separation factor of greater than about 100 with respect to the feed stream.

Claim 20

The membrane system of claim 17 in which said separation factor is greater than about 1,000.

Claim 21

The membrane system of claim 16 in which said conduit means for purge gas is such as to provide a cleaning ratio of from about 0.6 to about 1.7.

Claim 22

The membrane system of claim 19 in which said cleaning ratio is greater than unity.

Claim 23

The membrane system of claim 16 in which said hollow fibers are helically wound, with the active length thereof being essentially uniform, thus enabling said essentially uniform flow of gas across both sides of the membrane comprising said substrate portion and a skin or separation layer portion thereof to be facilitated.

Claim 24

The membrane system of claim 16 in which said means to establish a countercurrent flow pattern across the surfaces of the membrane comprise an impervious barrier that encases the membrane along the longitudinal outer surface thereof.

Claim 25

The membrane system of claim 16 in which said surface porosity is greater than 0.5%.

Claim 26

The membrane system of claim 23 in which said surface porosity is from about 0.5% to about 5% or more.

Claim 27

The membrane system of claim 16 in which said membrane system comprises a composite membrane system.

Claim 28

The membrane system of claim 25 in which said substrate comprises polysulfone.

Claim 29

The membrane system of claim 16 in which said membrane system comprises an asymmetric membrane system.