US4881954A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Permeable membranes for enhanced gas separation
Assignee: Praxair Technology Inc
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Filing: 1987-07-31
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Granted: 1989-11-21
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Expires: 2007-07-31
Abstract
Abstract Composite membranes are prepared by depositing a separation layer on an asymmetric support layer. The separation layer has a selectivity equal to or greater than that of the material of the asymmetric support layer for a desired gas separation. The support layer is desirably produced in non-asymmetric form, and exposed to an elevated temperature approaching the glass transition temperature of the support layer material under non-swelling conditions to modify the structure thereof to create asymmetry therein, before or after the deposition of the separation layer, and to increase its compaction resistance and collapse pressure. Such desirable properties are conveniently achieved on a repeatable basis, enhancing the uniformity and reliability of the treated support layer and of composite membranes produced therefrom, for use in gas separation operations.
Inventors
- 👤 Benjamin Bikson
- 👤 James E. Miller
- 👤 Joyce K. Nelson
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 13:55
CPC Classifications
B; B01; B01D; B01D71/00; B01D71/06; B01D71/66; B01D71/68; B01D67/00; B01D67/0081; B01D67/0083; B01D53/00; B01D53/22; B01D53/228; B01D69/00; B01D69/12
Claims Analysis
Total Claims: 26
Claim 1
Independent Claim
304 words
In the process for the separation of a more readily permeable component of a feed gas mixture from a less readily permeable component thereof by contacting said feed gas mixture with the feed side of a composite membrane having gas separation characteristics, and separately withdrawing the more readily permeable component from the composite membrane as a permeate stream and said less readily permeable component as a non-permeate stream, the improvement comprising employing a composite membrane comprising: (a) a porous polymeric support layer in asymmetric form, having a relatively thin, dense, semipermeable outer skin region and a less dense, porous non-selective support region that serves to preclude the collapse of the skin region under pressure, said skin region being capable of selectively permeating a more readily permeable component of the feed gas mixture to be separated at a desirably high permeation rate, wherein said porous support layer, after being produced in a desired porous form, washed and dried, is exposed in essentially dry form to an elevated temperature approaching the glass transition temperature of the material of the support layer under non-swelling conditions for a period of time sufficient to modify the porous support layer to form asymmetry therein, with increased compaction resistance and collapse pressure, said time being insufficient to cause the collapse of said support layer; and (b) a separation layer deposited on the outer skin region of said support layer without alteration of the structure of said support layer, said separation layer having a selectivity for said more readily permeable component greater than that of the material of the asymmetric support layer, the resulting composite membrane exhibiting separation characteristics equal to or higher than the intrinsic separation characteristics of the material of the asymmetric support layer, whereby said composite membrane exhibits enhanced gas permeability and separation characteristics in desired gas separation operations.
Claim 2
Dependent Claim
304 words
In the process for the separation of a more readily permeable component of a feed gas mixture from a less readily permeable component thereof by contacting said feed gas mixture with the feed side of a composite membrane having gas separation characteristics, and separately withdrawing the more readily permeable component from the composite membrane as a permeate stream and said less readily permeable component as a non-permeate stream, the improvement comprising employing a composite membrane comprising: (a) a porous polymeric support layer in asymmetric form, having a relatively thin, dense, semipermeable outer skin region and a less dense, porous non-selective support region that serves to preclude the collapse of the skin region under pressure, said skin region being capable of selectively permeating a more readily permeable component of the feed gas mixture to be separated at a desirably high permeation rate, wherein said porous support layer, after being produced in a desired porous form, washed and dried, is exposed in essentially dry form to an elevated temperature approaching the glass transition temperature of the material of the support layer under non-swelling conditions for a period of time sufficient to modify the porous support layer to form asymmetry therein, with increased compaction resistance and collapse pressure, said time being insufficient to cause the collapse of said support layer; and (b) a separation layer deposited on the outer skin region of said support layer without alteration of the structure of said support layer, said separation layer having a selectivity for said more readily permeable component greater than that of the material of the asymmetric support layer, the resulting composite membrane exhibiting separation characteristics equal to or higher than the intrinsic separation characteristics of the material of the asymmetric support layer, whereby said composite membrane exhibits enhanced gas permeability and separation characteristics in desired gas separation operations.
Claim 3
Dependent Claim
15 words
The process of claim 1 in which said non-swelling conditions comprise a heated gas atmosphere.
Claim 4
Dependent Claim
21 words
The process of claim 1 in which said support layer comprises polysulfone and said composite membrane is in hollow fiber form.
Claim 5
Dependent Claim
232 words
A composite membrane having enhanced gas separation characteristics comprising: (a) a porous support layer in asymmetric form, having a relatively thin, dense semipermeable skin region and a less dense, porous non-selective support region that serves to preclude the collapse of the skin region under pressure, said skin region being capable of selectively permeating a more readily permeable component of a feed gas mixture to be separated said support layer, after being formed, in a desired porous form, washed and dried, being exposed in essentially dry form to an elevated temperature approaching the glass transition temperature of the support layer material under non-swelling conditions for a short period of time sufficient to modify the membrane structure to create asymmetry therein and to increase its compaction resistance and collapse pressure, without causing the collapse of said membrane; and (b) a separation layer deposited on the outer surface of said skin region, said separation layer having a selectivity for said more readily permeable component equal to or greater than that of the skin region of said asymmetric support layer, said separation layer thus determining the separation characteristics of the composite membrane, whereby said composite membrane exhibits enhanced selectivity and permeability characteristics, and advantageous combinations of selectivity and permeability, together with desirable compaction resistance and collapse pressure on a repeatable basis, enhancing the uniformity and reliability of the composite membrane for use in gas separation operations.
Claim 6
Dependent Claim
232 words
A composite membrane having enhanced gas separation characteristics comprising: (a) a porous support layer in asymmetric form, having a relatively thin, dense semipermeable skin region and a less dense, porous non-selective support region that serves to preclude the collapse of the skin region under pressure, said skin region being capable of selectively permeating a more readily permeable component of a feed gas mixture to be separated said support layer, after being formed, in a desired porous form, washed and dried, being exposed in essentially dry form to an elevated temperature approaching the glass transition temperature of the support layer material under non-swelling conditions for a short period of time sufficient to modify the membrane structure to create asymmetry therein and to increase its compaction resistance and collapse pressure, without causing the collapse of said membrane; and (b) a separation layer deposited on the outer surface of said skin region, said separation layer having a selectivity for said more readily permeable component equal to or greater than that of the skin region of said asymmetric support layer, said separation layer thus determining the separation characteristics of the composite membrane, whereby said composite membrane exhibits enhanced selectivity and permeability characteristics, and advantageous combinations of selectivity and permeability, together with desirable compaction resistance and collapse pressure on a repeatable basis, enhancing the uniformity and reliability of the composite membrane for use in gas separation operations.
Claim 7
Dependent Claim
15 words
The composite membrane of claim 4 in which said membrane is in hollow fiber form.
Claim 8
Dependent Claim
13 words
The composite membrane of claim 5 in which said support layer comprises polysulfone.
Claim 9
Dependent Claim
15 words
The composite membrane of claim 4 in which said separation layer comprises a polymeric material.
Claim 10
Dependent Claim
14 words
The composite membrane of claim 7 in which said separation layer comprises cellulose acetate.
Claim 11
Dependent Claim
13 words
The composite membrane of claim 7 in which said separation layer comprises polyarylate.
Claim 12
Dependent Claim
14 words
The composite membrane of claim 9 in which said separation layer comprises sulfonated polysulfone.
Claim 13
Dependent Claim
14 words
The composite membrane of claim 9 in which said separation layer comprises brominated polyphenyleneoxide.
Claim 14
Dependent Claim
13 words
The composite membrane of claim 4 in which said support layer comprises polysulfone.
Claim 15
Dependent Claim
38 words
The composite membrane of claim 4 in which said non swelling conditions comprise a heated as atmosphere at a temperature of not more than about 20° C. less than said glass transition temperature of the support layer material.
Claim 16
Dependent Claim
44 words
The composite membrane of claim 13 in which said support layer comprises polysulfone and said heated gas atmosphere comprises hot, essentially dry air, said support layer being exposed to said elevated temperature for a period of from about 5 seconds to about 5 minutes.
Claim 17
Dependent Claim
45 words
The composite membrane of claim 4 in which the support layer is exposed to said elevated temperature under non-swelling conditions by passing the membrane through a bath on non-swelling liquid for a period of time not sufficient to cause the collapse of said support layer.
Claim 18
Dependent Claim
14 words
The composite membrane of claim 15 in which said support layer comprises polysulfone in
Claim 19
Dependent Claim
242 words
In the process of preparing a composite polymeric membrane capable of selectively permeating a more readily permeable component of a feed gas mixture, said composite membrane comprising a porous support layer in asymmetric form, having a relatively thin, dense semipermeable outer skin region and a less dense, porous non-selective support region, and a separation layer, deposited on the outer skin region of the support layer, wherein said porous support layer is produced in a desired porous form, washed and dried, the improvement comprising: (a) exposing said porous support layer in essentially dry form to an elevated temperature approaching the glass transition temperature of the material of said support layer under non-swelling conditions for a period of time sufficient to modify the porous support layer to form asymmetry therein, with increased compaction resistance and collapse pressure, said time being insufficient to cause the collapse of said support layer; and (b) depositing a separation material on the support layer, prior to, or after, the treatment of step (a) forming asymmetry in said support layer, so as to form a separation layer thereon, said separation layer having a selectivity for the more readily permeable component of the gas mixture to be separated that is equal to or greater than the intrinsic separation characteristics of the material of said support layer, whereby the uniformity and reliability of the treated asymmetric support layer, and of the resulting composite membrane, is enhanced for use in gas separation operations.
Claim 20
Dependent Claim
242 words
In the process of preparing a composite polymeric membrane capable of selectively permeating a more readily permeable component of a feed gas mixture, said composite membrane comprising a porous support layer in asymmetric form, having a relatively thin, dense semipermeable outer skin region and a less dense, porous non-selective support region, and a separation layer, deposited on the outer skin region of the support layer, wherein said porous support layer is produced in a desired porous form, washed and dried, the improvement comprising: (a) exposing said porous support layer in essentially dry form to an elevated temperature approaching the glass transition temperature of the material of said support layer under non-swelling conditions for a period of time sufficient to modify the porous support layer to form asymmetry therein, with increased compaction resistance and collapse pressure, said time being insufficient to cause the collapse of said support layer; and (b) depositing a separation material on the support layer, prior to, or after, the treatment of step (a) forming asymmetry in said support layer, so as to form a separation layer thereon, said separation layer having a selectivity for the more readily permeable component of the gas mixture to be separated that is equal to or greater than the intrinsic separation characteristics of the material of said support layer, whereby the uniformity and reliability of the treated asymmetric support layer, and of the resulting composite membrane, is enhanced for use in gas separation operations.
Claim 21
Dependent Claim
33 words
The process of claim 17 in which said separation material is deposited on the outer skin region of the support layer following said treatment step (a) to form asymmetry in said support layer.
Claim 22
Dependent Claim
30 words
The process of claim 17 in which said separation material is deposited on the porous support layer prior to said treatment step (a) to form asymmetry in said support layer.
Claim 23
Dependent Claim
28 words
The process of claim 17 in which said exposure to said elevated temperature under non-swelling conditions comprising passing said porous support layer through a bath of non-swelling liquid.
Claim 24
Dependent Claim
17 words
The process of claim 17 in which said asymmetric treated membrane comprises polysulfone in hollow fiber form.
Claim 25
Dependent Claim
15 words
The process of claim 21 in which said non-swelling conditions comprise a hot air atmosphere.
Claim 26
Dependent Claim
15 words
The process of claim 21 in which said non-swelling conditions comprise an inert gas atmosphere.
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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 |