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US4881955A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for gas separation using helically wound hollow fibers permeable membrane cartridge

Assignee: LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
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Filing: 1988-09-12
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Granted: 1989-11-21
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Expires: 2008-09-12
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Abstract

Abstract Feed gas is introduced into the bores of a helically wound hollow fiber membrane cartridge containing hollow fibers of essentially uniform active lengths. Permeate gas flow is maintained countercurrent to the feed and raffinate gas entrance and exit axis, respectively, while the directional flow axis of permeate withdrawal can be at a substantial angle to the helically wound hollow fiber membrane surface. Complete radial mixing of the permeate stream on the outer, permeate side and essentially no axial mixing on either the permeate or the raffinate side of the hollow fiber membrane cartridge are maintained.

Inventors

  • 👤 Benjamin Bikson
  • 👤 Slavatore Giglia

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 08:23
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/22; B01D63/00; B01D63/02; B01D63/025; B01D63/10; B01D69/00; B01D69/12; B01D69/1213; B01D71/00; B01D71/06; B01D71/08; B01D71/12; B01D71/22; B01D71/66; B01D71/68; B01D2313/00; B01D2313/44

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 255 words
A gas separation process for the separation of at least one fast gas component from a feed gas mixture containing such fast gas component and at least one other gaseous component in a permeator module containing a helically wound hollow fiber cartridge, said process comprising: (a) passing the feed gas mixture to the permeator module so as to pass through the bores of the hollow fibers in said helically wound hollow fiber cartridge from a first feed end thereof, all of the hollow fibers in said permeable membrane cartridge being essentially of uniform length; (b) recovering said fast gas component that permeates the hollow fibers as a permeate stream on the outer, permeate side of said hollow fibers, said permeate stream being passed from the permeator module in a permeate flow direction that is countercurrent to the direction of the feed gas mixture flow within the bores of the hollow fibers; and (c) recovering a raffinate stream from the permeator module, said raffinate stream leaving the bores of the hollow fibers through a second, exit end thereof opposite the feed end thereof, said raffinate stream passing in a flow direction that is cocurrent to the direction of feed gas mixture flow within the bores of the hollow fibers, thereby maintaining (i) significant radial mixing of the permeate stream on the outer, permeate side of the hollow fiber permeable membrane cartridge and (ii) essentially no axial mixing on either (a) the outer permeate side or (b) in the bores of said hollow fiber permeable membrane cartridge.
Claim 2
Dependent Claim 255 words
A gas separation process for the separation of at least one fast gas component from a feed gas mixture containing such fast gas component and at least one other gaseous component in a permeator module containing a helically wound hollow fiber cartridge, said process comprising: (a) passing the feed gas mixture to the permeator module so as to pass through the bores of the hollow fibers in said helically wound hollow fiber cartridge from a first feed end thereof, all of the hollow fibers in said permeable membrane cartridge being essentially of uniform length; (b) recovering said fast gas component that permeates the hollow fibers as a permeate stream on the outer, permeate side of said hollow fibers, said permeate stream being passed from the permeator module in a permeate flow direction that is countercurrent to the direction of the feed gas mixture flow within the bores of the hollow fibers; and (c) recovering a raffinate stream from the permeator module, said raffinate stream leaving the bores of the hollow fibers through a second, exit end thereof opposite the feed end thereof, said raffinate stream passing in a flow direction that is cocurrent to the direction of feed gas mixture flow within the bores of the hollow fibers, thereby maintaining (i) significant radial mixing of the permeate stream on the outer, permeate side of the hollow fiber permeable membrane cartridge and (ii) essentially no axial mixing on either (a) the outer permeate side or (b) in the bores of said hollow fiber permeable membrane cartridge.
Claim 3
Dependent Claim 32 words
A gas separation process as claimed in claim 1, wherein the lengths of the hollow fibers comprising the hollow fiber permeable membrane cartridge vary from one another by less than about 10%.
Claim 4
Dependent Claim 35 words
A gas separation process as claimed in claim 1, wherein the lengths of the hollow fibers comprising the hollow fiber permeable membrane cartridge vary from one another by less than about 5% to about 10%.
Claim 5
Dependent Claim 20 words
A gas separation process as claimed in claim 1, wherein said hollow fiber permeable membrane membrane is a composite membrane.
Claim 6
Dependent Claim 16 words
A gas separation process as claimed in claim 4, wherein said hollow fiber is coated polysulfone.
Claim 7
Dependent Claim 21 words
A gas separation process as claimed in claim 4, wherein said composite membranre is polysulfone hollow fiber coated with ethyl cellulose.
Claim 8
Dependent Claim 16 words
A gas separation process as claimed in claim 1, wherein the feed gas mixture is air.
Claim 9
Dependent Claim 27 words
A gas separation process as claimed in claim 1, wherein the feed gas is at essentially atmospheric pressure and the permeate is withdrawn under reduced atmospheric pressure.
Claim 10
Dependent Claim 32 words
A gas separation process as claimed in claim 1 wherein the feed gas mixture is passed to the permeator module at a pressure of from about 50 psig to about 400 psig.
Claim 11
Dependent Claim 208 words
A gas separation process for the separation of at least one fast gas component from a feed gas mixture containing said fast gas component and at least one other gaseous component in a permeator module containing a helically wound hollow fiber cartridge, said process comprising: (a) passing the feed gas mixture to the premeator module so as to pas through the bores of the hollow fibers in said helically wound hollow fiber cartridge from a first feed end thereof, all of the hollow fibers in said permeable membrane cartridge being essentially of uniform length; (b) recovering said fast gas component that permeates the hollow fibers as a permeate stream on the outer, permeate side of said hollow fibers, said permeate stream being passed from the permeator module in a permeate flow direction that is countercurrent to the direction of the feed gas mixture flow within the bores of the hollow fibers; and (c) recovering a raffinate stream from the permeator module, said raffinate stream leaving the bores of the hollow fibers through a second, exit end thereof opposite the feed end thereof, said raffinate stream passing in a flow direction that is cocurrent to the direction of feed gas mixture flow within the bores of the hollow fibers.
Claim 12
Dependent Claim 208 words
A gas separation process for the separation of at least one fast gas component from a feed gas mixture containing said fast gas component and at least one other gaseous component in a permeator module containing a helically wound hollow fiber cartridge, said process comprising: (a) passing the feed gas mixture to the premeator module so as to pas through the bores of the hollow fibers in said helically wound hollow fiber cartridge from a first feed end thereof, all of the hollow fibers in said permeable membrane cartridge being essentially of uniform length; (b) recovering said fast gas component that permeates the hollow fibers as a permeate stream on the outer, permeate side of said hollow fibers, said permeate stream being passed from the permeator module in a permeate flow direction that is countercurrent to the direction of the feed gas mixture flow within the bores of the hollow fibers; and (c) recovering a raffinate stream from the permeator module, said raffinate stream leaving the bores of the hollow fibers through a second, exit end thereof opposite the feed end thereof, said raffinate stream passing in a flow direction that is cocurrent to the direction of feed gas mixture flow within the bores of the hollow fibers.
Claim 13
Dependent Claim 233 words
A gas separation process for the separation of at least one fast gas component from a feed gas mixture containing said fast gas component and at least one other gaseous component in a permeator module containing a helically wound hollow fiber cartridge, said process comprising: (a) passing the feed gas mixture to the permeator module so as to pass through the bores of the hollow fibers in said helically wound hollow fiber cartridge from a first feed end thereof, all of the hollow fibers in said permeable membrane cartridge being essentially of uniform length; (b) recovering said fast gas component that permeates the hollow fibers as a permeate stream on the outer, permeate side of said hollow fibers, said permeate stream being passed from the permeator module in a permeate flow direction that is countercurrent to the direction of the feed gas mixture flow within the bores of the hollow fibers; and (c) recovering a raffinate stream from the permeator module, said raffinate stream leaving the bores of the hollow fibers through a second, exit end thereof opposite the feed end thereof, said raffinate stream passing in a flow direction that is cocurrent to the direction of feed gas mixture flow within the bores of the hollow fibers, thereby maintaining essentially no axial mixing on either (a) the outer, permeate side or (b) in the bores of said hollow fiber permeable membrane cartridge.
Claim 14
Dependent Claim 233 words
A gas separation process for the separation of at least one fast gas component from a feed gas mixture containing said fast gas component and at least one other gaseous component in a permeator module containing a helically wound hollow fiber cartridge, said process comprising: (a) passing the feed gas mixture to the permeator module so as to pass through the bores of the hollow fibers in said helically wound hollow fiber cartridge from a first feed end thereof, all of the hollow fibers in said permeable membrane cartridge being essentially of uniform length; (b) recovering said fast gas component that permeates the hollow fibers as a permeate stream on the outer, permeate side of said hollow fibers, said permeate stream being passed from the permeator module in a permeate flow direction that is countercurrent to the direction of the feed gas mixture flow within the bores of the hollow fibers; and (c) recovering a raffinate stream from the permeator module, said raffinate stream leaving the bores of the hollow fibers through a second, exit end thereof opposite the feed end thereof, said raffinate stream passing in a flow direction that is cocurrent to the direction of feed gas mixture flow within the bores of the hollow fibers, thereby maintaining essentially no axial mixing on either (a) the outer, permeate side or (b) in the bores of said hollow fiber permeable membrane cartridge.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1992-11-20 1993-05-22 1993-11-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1996-11-20 1997-05-22 1997-11-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2000-11-20 2001-05-22 2001-11-21 $7700.00 Window Closed / Lapsed

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