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US4871378A Expired / Lapsed US ⏱️ 0.0 years remaining

Ultrathin ethylcellulose/poly(4-methylpentene-1) permselective membranes

Assignee: Membrane Technology and Research Inc
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Filing: 1987-12-11
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Granted: 1989-10-03
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Expires: 2007-12-11
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Abstract

Abstract An ultrathin, permselective membrane for use in gas or vapor separations. The membrane comprises a permselective layer of ethylcellulose in combination with one or more permselective layers of poly(4-methylpentene-1). The permselective membrane is preferably coated onto a microporous substrate, such as an asymmetric Loeb-Sourirajan type membrane. The resulting membrane has high gas fluxes and selectivities, and can be used, for example, to separate oxygen and nitrogen; hydrogen sulfide from nitrogen, methane or carbon dioxide; hydrogen from nitrogen; sulfur dioxide or ammonia from nitrogen; or water vapor from air. A method of preparing such a membrane is also provided, as is a gas separation process using the membrane.

Inventors

  • 👤 Ingo Pinnau

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 15:45
CPC Classifications
B; B01; B01D; B01D71/00; B01D71/06; B01D71/08; B01D71/12; B01D71/22; B01D69/00; B01D69/10; B01D69/106; B01D69/12; B01D69/1216

Claims Analysis

Total Claims: 15
Claim 1
Independent Claim 91 words
A membrane useful for gas separation, comprising: an ultrathin, permselective ethylcellulose layer having the general formula ##STR5## wherein the ethoxyl content is in the range 35% to 50%; and an ultrathin, permselective poly(4-methylpentene-1) layer having the formula ##STR6## said poly(4-methylpentene-1) layer forming a coating on one surface of said ethylcellulose layer, said membrane having an O 2 /N 2 selectivity which is greater than the intrinsic O 2 /N 2 selectivity of said ethylcellulose and which is greater than 90% of the intrinsic O 2 /N 2 selectivity of said poly(4-methylpentene-1).
Claim 2
Dependent Claim 91 words
A membrane useful for gas separation, comprising: an ultrathin, permselective ethylcellulose layer having the general formula ##STR5## wherein the ethoxyl content is in the range 35% to 50%; and an ultrathin, permselective poly(4-methylpentene-1) layer having the formula ##STR6## said poly(4-methylpentene-1) layer forming a coating on one surface of said ethylcellulose layer, said membrane having an O 2 /N 2 selectivity which is greater than the intrinsic O 2 /N 2 selectivity of said ethylcellulose and which is greater than 90% of the intrinsic O 2 /N 2 selectivity of said poly(4-methylpentene-1).
Claim 3
Dependent Claim 24 words
The membrane of claim 1, further comprising a microporous support membrane, said ethylcellulose layer forming a coating on one side of said support membrane.
Claim 4
Dependent Claim 15 words
The membrane of claim 1, wherein said ethylcellulose layer is less than 2 microns thick.
Claim 5
Dependent Claim 15 words
The membrane of claim 1, wherein said poly(4-methylpentene-1) layer is less than 2 microns thick.
Claim 6
Dependent Claim 72 words
A process for separating a gas A from a gas B in a first gas mixture containing A and B, comprising the steps of: contacting the feed side of the membrane of claim 1 with said gas mixture; and withdrawing from the permeate side of said membrane a second gas mixture wherein the proportion of gas A is enriched, and the proportion of gas B depleted, compared to said first gas mixture.
Claim 7
Dependent Claim 132 words
A process for producing a membrane useful for gas separation comprising the steps of: preparing an ethylcellulose solution from ethylcellulose having the general formula ##STR7## wherein the ethoxyl content is in the range 35% to 50%; coating said ethylcellulose solution onto a support; drying said coated support, to produce a first ultrathin, permselective layer of ethylcellulose; preparing a poly(4-methylpentene-1) solution from poly(4methylpentene-1) having the formula ##STR8## coating said poly(4-methylpentene-1) solution onto said coated support; and drying said coated support, to produce a second ultrathin, permselective layer of poly(4-methylpentene-1, whereby a composite membrane, having an O 2 /N 2 selectivity which is greater than the intrinsic O 2 /N 2 selectivity of said ethylcellulose and which is greater than 90% of the intrinsic O 2 /N 2 selectivity of said poly(4-methylpentene-1), is formed.
Claim 8
Dependent Claim 132 words
A process for producing a membrane useful for gas separation comprising the steps of: preparing an ethylcellulose solution from ethylcellulose having the general formula ##STR7## wherein the ethoxyl content is in the range 35% to 50%; coating said ethylcellulose solution onto a support; drying said coated support, to produce a first ultrathin, permselective layer of ethylcellulose; preparing a poly(4-methylpentene-1) solution from poly(4methylpentene-1) having the formula ##STR8## coating said poly(4-methylpentene-1) solution onto said coated support; and drying said coated support, to produce a second ultrathin, permselective layer of poly(4-methylpentene-1, whereby a composite membrane, having an O 2 /N 2 selectivity which is greater than the intrinsic O 2 /N 2 selectivity of said ethylcellulose and which is greater than 90% of the intrinsic O 2 /N 2 selectivity of said poly(4-methylpentene-1), is formed.
Claim 9
Dependent Claim 18 words
The process as in claim 6, wherein said ethylcellulose solution contains a maximum ethylcellulose concentration of 5 wt%.
Claim 10
Dependent Claim 18 words
The process as in claim 6, wherein said ethylcellulose solution contains a maximum ethylcellulose concentration of 2 wt%.
Claim 11
Dependent Claim 34 words
The process as in claim 6, wherein said ethylcellulose solution comprises ethylcellulose having the general formula ##STR9## wherein the ethoxyl content is in the range 35% to 50%, dissolved in a monohydric aliphatic alcohol.
Claim 12
Dependent Claim 13 words
The process as in claim 9, wherein said monohydric aliphatic alcohol is 2-propanol.
Claim 13
Dependent Claim 18 words
The process as in claim 6, wherein said poly(4-methylpentene-1) solution contains a maximum poly(4-methylpentene-1) concentration of 5 wt%.
Claim 14
Dependent Claim 18 words
The process as in claim 6, wherein said poly(4-methylpentene-1) solution contains a maximum poly(4-methylpentene-1) concentration of 2 wt%.
Claim 15
Dependent Claim 15 words
The process as in claim 6, wherein said poly(4-methylpentene-1) solution comprises poly(4-methylpentene-1) dissolved in cyclohexane.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1992-10-02 1993-04-03 1993-10-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1996-10-02 1997-04-03 1997-10-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2000-10-02 2001-04-03 2001-10-03 $7700.00 Window Closed / Lapsed

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