US4780205A
Expired / Lapsed
US
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Permselective hollow fiber membrane, process for the preparation thereof, method and apparatus for plasma components separation
Assignee: Teijin Ltd
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Filing: 1985-10-30
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Granted: 1988-10-25
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Expires: 2005-10-30
Abstract
Abstract A permselective hollow fiber membrane which is a hollow fiber membrane, made from a wet spinnable organic high polymer, having a dense skin layer of gelated structure made to a thickness of 1μ or less on at least one surface of the membrane and the rest being made up into a porous layer, a process for the preparation thereof, a method and an apparatus of plasma components separation in which said hollow fiber membrane is used.
Inventors
- 👤 Eiichi Murakami
- 👤 Kimihiko Matsuzawa
- 👤 Eiji Masunaga
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 02:21
CPC Classifications
B; B01; B01D; B01D67/00; B01D67/0081; B01D67/0088; B01D69/00; B01D69/02; B01D69/08
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
234 words
An apparatus for plasma components separation comprising a separating means consisting of hollow fiber membranes having every property required for carrying out plasmapheresis including a high albumin recovery ratio, a high ratio of IgM removal and a little-lowering of separation efficiency to clogging developed on the hollow fiber membrane, a chamber to house these membranes, an inlet means to draw in a liquid material which contains plasma components, an outlet means to allow the filtrate to flow out, and another outlet means to allow the unpermeated residual liquid material to flow out, thus forming an apparatus of hollow fiber membrane type for separating plasma components which is characterized by having, as a separating means, a permselective hollow fiber membrane, made from a wet spinnable organic high polymer, having a dense skin layer of gelated structure made to a thickness of 1 μ or less on at least one surface of the membrane and the rest being made up into a porous layer, made to have the ultrafiltration rate of water ranging from 50 to 350 ml/m 2 .hr.mmHg, and also, in the continuous filtration of human plasma components, made to have the albumin permeation rate of more than 80%, the immunoglobulin M rejection rate of more than 70%, and the total amount of the filtrate of more than 3 l per 1 m 2 of the effective surface area of the hollow fiber membrane.
Claim 2
Independent Claim
234 words
An apparatus for plasma components separation comprising a separating means consisting of hollow fiber membranes having every property required for carrying out plasmapheresis including a high albumin recovery ratio, a high ratio of IgM removal and a little-lowering of separation efficiency to clogging developed on the hollow fiber membrane, a chamber to house these membranes, an inlet means to draw in a liquid material which contains plasma components, an outlet means to allow the filtrate to flow out, and another outlet means to allow the unpermeated residual liquid material to flow out, thus forming an apparatus of hollow fiber membrane type for separating plasma components which is characterized by having, as a separating means, a permselective hollow fiber membrane, made from a wet spinnable organic high polymer, having a dense skin layer of gelated structure made to a thickness of 1 μ or less on at least one surface of the membrane and the rest being made up into a porous layer, made to have the ultrafiltration rate of water ranging from 50 to 350 ml/m 2 .hr.mmHg, and also, in the continuous filtration of human plasma components, made to have the albumin permeation rate of more than 80%, the immunoglobulin M rejection rate of more than 70%, and the total amount of the filtrate of more than 3 l per 1 m 2 of the effective surface area of the hollow fiber membrane.
Claim 3
Dependent Claim
173 words
A permselective hollow fiber membrane which comprises a hollow fiber membrane having every property required for carrying out plasmapheresis including a high albumin recovery ratio, a high ratio of IgM removal and a little-lowering of separation efficiency to clogging developed on the hollow fiber membrane, made of a wet spinnable organic high polymer, consisting of a dense skin layer having thickness of less than 1 μ with a gelated structure formed on at least one surface of the hollow fiber membrane, and a porous layer, made to have ultrafiltration rate of water raning from 50 to 350 ml/m 2 .hr.mmHg, and also, in continuous filtration of human plasma components by feeding continuously fresh human blood plasma at the surface having said dense skin layer and discarding continuously filtrate, made to maintain albumin permeation ratio of more than 80% and immunoglobulin M rejection ratio of more than 70%, and to have total amount of said filtrate of more than 3 l per 1 m 2 or effective surface area of the hollow fiber membrane.
Claim 4
Dependent Claim
173 words
A permselective hollow fiber membrane which comprises a hollow fiber membrane having every property required for carrying out plasmapheresis including a high albumin recovery ratio, a high ratio of IgM removal and a little-lowering of separation efficiency to clogging developed on the hollow fiber membrane, made of a wet spinnable organic high polymer, consisting of a dense skin layer having thickness of less than 1 μ with a gelated structure formed on at least one surface of the hollow fiber membrane, and a porous layer, made to have ultrafiltration rate of water raning from 50 to 350 ml/m 2 .hr.mmHg, and also, in continuous filtration of human plasma components by feeding continuously fresh human blood plasma at the surface having said dense skin layer and discarding continuously filtrate, made to maintain albumin permeation ratio of more than 80% and immunoglobulin M rejection ratio of more than 70%, and to have total amount of said filtrate of more than 3 l per 1 m 2 or effective surface area of the hollow fiber membrane.
Claim 5
Dependent Claim
25 words
A permselective hollow fiber membrane according to claim 2 wherein said dense skin layer is formed on the outer surface of the hollow fiber membrane.
Claim 6
Dependent Claim
26 words
A permselective hollow fiber membrane according to claim 2, wherein immunoglobulin G rejection rate is more than 20% in said continuous filtration of human plasma components.
Claim 7
Dependent Claim
26 words
A permselective hollow fiber membrane according to claim 1, wherein said ultrafiltration rate for water is in the range of 150 to 350 ml/m 2 .hr.mmHg.
Claim 8
Dependent Claim
26 words
A permselective hollow fiber membrane according to claim 1, wherein transmembrane pressure difference is less than 100 mmHg in said continuous filtration of human plasma components.
Claim 9
Dependent Claim
44 words
A permselective hollow fiber membrane according to claim 1, wherein permeation ratio of dextran is in the range of 20 to 70% determined in permeation of an aqueous solution containing dextran of weight average molecular weight of 500,000 at a rate of 50 mg/dl.
Claim 10
Dependent Claim
35 words
A permselective hollow fiber membrane according to claim 1, wherein said organic high polymer is at least one kind of polymer selected from cellulose ester, polymethyl methacrylate, polyvinyl alcohol, ethylene-vinyl alcohol copolymer, polyacrylonitrile, and polysufone.
Claim 11
Independent Claim
231 words
An apparatus for plasma components separation comprising a chamber having inlet means to receive liquid material which contains plasma components, outlet means to allow filtrate to flow out of said chamber and other outlet means to allow unpermeated residual liquid material to flow out of said chamber, and containing mounted in said chamber permselective hollow fiber membranes having every property required for carrying out plasmapheresis including a high albumin recovery ratio, a high ratio of IgM removal and a little-lowering of separation efficiency to clogging developed on the hollow fiber membrane, wherein each of said permselective hollow fiber membranes comprises a hollow fiber membrane made of a wet spinnable organic high polymer, consisting of a dense skin layer having thickness of less than 1μ with a gelated structure formed on at least one surface of the hollow fiber membrane, and a porous layer, made to have ultrafiltration rate of water ranging from 50 to 350 ml/m 2 .hr.mmHg, and also, in continuous filtration of human plasma components by feeding continuously fresh human blood plasma at the surface having said dense skin layer and discarding continuously filtrate, made to maintain albumin permeation ratio of more than 80% and immunoglobulin M rejection ratio of more than 70%, and to have total amount of said filtrate of more than 3 l per 1 m 2 of effective surface area of the hollow fiber membrane.
Claim 12
Independent Claim
231 words
An apparatus for plasma components separation comprising a chamber having inlet means to receive liquid material which contains plasma components, outlet means to allow filtrate to flow out of said chamber and other outlet means to allow unpermeated residual liquid material to flow out of said chamber, and containing mounted in said chamber permselective hollow fiber membranes having every property required for carrying out plasmapheresis including a high albumin recovery ratio, a high ratio of IgM removal and a little-lowering of separation efficiency to clogging developed on the hollow fiber membrane, wherein each of said permselective hollow fiber membranes comprises a hollow fiber membrane made of a wet spinnable organic high polymer, consisting of a dense skin layer having thickness of less than 1μ with a gelated structure formed on at least one surface of the hollow fiber membrane, and a porous layer, made to have ultrafiltration rate of water ranging from 50 to 350 ml/m 2 .hr.mmHg, and also, in continuous filtration of human plasma components by feeding continuously fresh human blood plasma at the surface having said dense skin layer and discarding continuously filtrate, made to maintain albumin permeation ratio of more than 80% and immunoglobulin M rejection ratio of more than 70%, and to have total amount of said filtrate of more than 3 l per 1 m 2 of effective surface area of the hollow fiber membrane.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
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| 3.5 Years (Year 4) | 1991-10-25 | 1992-04-25 | 1992-10-25 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-10-25 | 1996-04-25 | 1996-10-25 | $3760.00 | Window Closed / Lapsed |
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