US4264338A
Expired / Lapsed
US
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Method for separating gases
Assignee: Permea Inc
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Filing: 1979-08-16
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Granted: 1981-04-28
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Expires: 1999-08-16
Abstract
Abstract An improved process for the separation of gases by selective membrane diffusion or permeation by means of plural stages of membrane separation without increasing the work required by directing a permeant mixture from a second or later stage of separation to a recycle stage of membrane separation to provide a permeate enriched in the desired gas or gases and blending said permeate with the gaseous feed to said second or later stage of separation.
Inventors
- 👤 Harold R. Null
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 00:35
CPC Classifications
C; C01; C01B; C01B13/00; C01B13/02; C01B13/0229; C01B13/0248; C01B13/0251; B; B01; B01D; B01D53/00; B01D53/22; B01D53/225; B01D53/226; B01D59/00; B01D59/10; B01D59/12; B01D59/14; C01B3/00; C01B3/50; C01B3/501; C01B2203/00; C01B2203/04; C01B2203/0405; C01B2203/0465; C01B2203/047; C01B2203/0475; C01B2203/048; C01B2203/0485; C01B2210/00; C01B2210/0043; C01B2210/0046; C01B2210/0062
Claims Analysis
Total Claims: 23
Claim 1
Independent Claim
176 words
The method of separating gaseous mixtures characterized by (a) providing a pressurized initial gaseous mixture at superatmospheric pressure and contacting therewith a first stage membrane permeable to at least one of the gases in said mixture to provide an enriched first permeate mixture and a depleted first permeant mixture, (b) compressing said enriched first permeate mixture and contacting therewith a second stage membrane permeable to said at least one of the gases in said first permeate mixture to provide a further enriched second permeate mixture and a depleted second permeant mixture, (c) directing said depleted second permeant mixture, with no increase in pressure, into contact with a separate recycle stage membrane permeable to said at least one of the gases in said second permeant mixture to produce an enriched recycle permeate mixture and a depleted recycle permeant mixture, (d) blending said enriched recycle permeate mixture with said enriched first permeate mixture prior to the compression thereof, (e) blending said recycle permeant mixture with said pressurized initial gaseous mixture, and (f) recovering said enriched second permeate mixture.
Claim 2
Independent Claim
176 words
The method of separating gaseous mixtures characterized by (a) providing a pressurized initial gaseous mixture at superatmospheric pressure and contacting therewith a first stage membrane permeable to at least one of the gases in said mixture to provide an enriched first permeate mixture and a depleted first permeant mixture, (b) compressing said enriched first permeate mixture and contacting therewith a second stage membrane permeable to said at least one of the gases in said first permeate mixture to provide a further enriched second permeate mixture and a depleted second permeant mixture, (c) directing said depleted second permeant mixture, with no increase in pressure, into contact with a separate recycle stage membrane permeable to said at least one of the gases in said second permeant mixture to produce an enriched recycle permeate mixture and a depleted recycle permeant mixture, (d) blending said enriched recycle permeate mixture with said enriched first permeate mixture prior to the compression thereof, (e) blending said recycle permeant mixture with said pressurized initial gaseous mixture, and (f) recovering said enriched second permeate mixture.
Claim 3
Dependent Claim
17 words
The method of claim 1 characterized in that said depleted first permeant mixture is removed to disposal.
Claim 4
Dependent Claim
23 words
The method of claim 2 characterized in that said depleted first permeant mixture is expanded to a reduced pressure and power recovered therefrom.
Claim 5
Dependent Claim
37 words
The method of claim 1 characterized in that said recycle stage membrane is sized so as to produce a said enriched recycle permeate mixture of approximately the same composition of gases as said enriched first permeate mixture.
Claim 6
Dependent Claim
35 words
The method of claim 1 characterized in that said recycle stage membrane is sized so as to produce a depleted recycle permeant mixture of approximately the same composition of gases as said initial gaseous mixture.
Claim 7
Dependent Claim
22 words
The method of claim 1 characterized in that the said membranes permeable to said at least one gas are hollow fiber membranes.
Claim 8
Dependent Claim
23 words
The method of claim 1 characterized in that the said membranes permeable to said at least one gas are multicomponent hollow fiber membranes.
Claim 9
Dependent Claim
26 words
The method of claim 1 characterized in that said enriched second permeate mixture is subjected to additional stages of compression and separation prior to recovery thereof.
Claim 10
Dependent Claim
48 words
The method of claim 1 characterized in that said gaseous mixture comprises at least one gas and at least one other gas or vapor, and said at least one gas is separable from said at least one other gas or vapor by selective permeation through a semi-permeable membrane.
Claim 11
Independent Claim
187 words
The method for separating gaseous mixtures characterized by (a) subjecting a gaseous mixture to plural stages of contact at superatmospheric pressure with membranes permeable to at least one of the gases in said mixture to provide from a second or later stage of membrane separation a permeate mixture enriched in said at least one gas and a permeant mixture depleted in said at least one gas, (b) directing said permeant mixture from a second or later stage of membrane separation, with no increase in pressure, into contact with a separate recycle stage membrane permeable to said at least one gas to produce a recycle permeate mixture enriched in said at least one gas and a recycle permeant mixture depleted in said at least one gas, (c) blending said recycle permeate mixture with the permeate mixture from a preceding stage of membrane separation, (d) blending said recylce permeant mixture with the pressurized gaseous mixture fed to a preceding stage of membrane separation, and (e) subjecting said permeate mixture from said second or later stage of membrane separation to additional stages of compression and separation or to recovery thereof.
Claim 12
Independent Claim
187 words
The method for separating gaseous mixtures characterized by (a) subjecting a gaseous mixture to plural stages of contact at superatmospheric pressure with membranes permeable to at least one of the gases in said mixture to provide from a second or later stage of membrane separation a permeate mixture enriched in said at least one gas and a permeant mixture depleted in said at least one gas, (b) directing said permeant mixture from a second or later stage of membrane separation, with no increase in pressure, into contact with a separate recycle stage membrane permeable to said at least one gas to produce a recycle permeate mixture enriched in said at least one gas and a recycle permeant mixture depleted in said at least one gas, (c) blending said recycle permeate mixture with the permeate mixture from a preceding stage of membrane separation, (d) blending said recylce permeant mixture with the pressurized gaseous mixture fed to a preceding stage of membrane separation, and (e) subjecting said permeate mixture from said second or later stage of membrane separation to additional stages of compression and separation or to recovery thereof.
Claim 13
Independent Claim
208 words
The method for separating gaseous mixtures characterized by (a) subjecting a gaseous mixture to plural stages of contact at superatmospheric pressure with membranes permeable to at least one of the gases in said mixture to provide a penultimate permeate mixture enriched in said at least one gas and a penultimate permeant mixture depleted in said at least one gas, (b) compressing said enriched penultimate permeate mixture and contacting therewith a final stage membrane permeable to said at least one gas in said penultimate permeate mixture to provide a final stage permeate mixture further enriched in said at least one gas and a final stage permeant gas mixture depleted in said at least one gas, (c) directing said final stage permeant mixture, with no increase in pressure, into contact with a separate recycle stage membrane permeable to said at least one gas to produce a recycle permeate mixture enriched in said at least one gas and a recycle permeant mixture further depleted in said at least one gas, (d) blending said recycle permeate mixture with said penultimate permeate mixture prior to the compression thereof, (e) blending said recycle permeant mixture with the pressurized gaseous mixture fed to the penultimate stage membrane, and (f) recovering said final stage permeate mixture.
Claim 14
Independent Claim
208 words
The method for separating gaseous mixtures characterized by (a) subjecting a gaseous mixture to plural stages of contact at superatmospheric pressure with membranes permeable to at least one of the gases in said mixture to provide a penultimate permeate mixture enriched in said at least one gas and a penultimate permeant mixture depleted in said at least one gas, (b) compressing said enriched penultimate permeate mixture and contacting therewith a final stage membrane permeable to said at least one gas in said penultimate permeate mixture to provide a final stage permeate mixture further enriched in said at least one gas and a final stage permeant gas mixture depleted in said at least one gas, (c) directing said final stage permeant mixture, with no increase in pressure, into contact with a separate recycle stage membrane permeable to said at least one gas to produce a recycle permeate mixture enriched in said at least one gas and a recycle permeant mixture further depleted in said at least one gas, (d) blending said recycle permeate mixture with said penultimate permeate mixture prior to the compression thereof, (e) blending said recycle permeant mixture with the pressurized gaseous mixture fed to the penultimate stage membrane, and (f) recovering said final stage permeate mixture.
Claim 15
Dependent Claim
48 words
The method of claim 11 characterized in that said gaseous mixture comprises at least one gas and at least one other gas or vapor, and said at least one gas is separable from said at least one other gas or vapor by selective permeation through a semi-permeable membrane.
Claim 16
Dependent Claim
35 words
The method of claim 11 characterized in that said recycle stage membrane is sized so as to produce a said recycle permeate mixture of approximately the same composition of gases as said penultimate permeate mixture.
Claim 17
Dependent Claim
40 words
The method of claim 11 characterized in that said recycle stage membrane is sized so as to produce a said recycle permeant mixture of approximately the same composition of gases as said gaseous mixture fed to said penultimate stage membrane.
Claim 18
Dependent Claim
26 words
The method of claim 11 characterized in that said penultimate permeant mixture from (a) is blended with the gaseous mixture fed to a preceding stage membrane.
Claim 19
Dependent Claim
39 words
The method of claim 15 characterized in that said penultimate stage membrane is sized so as to produce said penultimate permeant mixture of approximately the same composition of gases as said gaseous mixture fed to said preceding stage membrane.
Claim 20
Dependent Claim
21 words
The method of claim 11 characterized in that said membranes permeable to said at least one gas are hollow fiber membranes.
Claim 21
Dependent Claim
22 words
The method of claim 11 characterized in that said membranes permeable to said at least one gas are multicomponent hollow fiber membranes.
Claim 22
Dependent Claim
31 words
The method of claim 11 characterized in that a permeant mixture from a stage of separation previous to said penultimate stage is expanded to a reduced pressure and power recovered therefrom.
Claim 23
Dependent Claim
48 words
The method of claim 10 characterized in that said gaseous mixture comprises at least one gas and at least one other gas or vapor, and said at least one gas is separable from said at least one other gas or vapor by selective permeation through a semi-permeable membrane.
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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) | 1984-04-27 | 1984-10-27 | 1985-04-28 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-04-27 | 1988-10-27 | 1989-04-28 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-04-27 | 1992-10-27 | 1993-04-28 | $7700.00 | Window Closed / Lapsed |