US4543221A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for making cellulose semipermeable hollow fibers
Assignee: Baxter International Inc
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Filing: 1981-10-21
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Granted: 1985-09-24
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Expires: 2001-10-21
Abstract
Abstract Improved cellulose semipermeable hollow fibers useful in detoxifying blood during hemodialysis or hemofiltration treatments. The cellulose fibers are fine, capillary fibers that are made by melt extrusion of certain cellulose ester polyol melt spin compositions into self-supporting gelled fibers. The cellulose ester gelled fibers are subsequently chemically converted into cellulose fibers by deacetylation, in aqueous alkali solution. The product fibers exhibit improved wet intrinsic tensile strength and higher water permeability characteristics than heretofore known cellulose fibers made from cellulose ester spin compositions. The invention includes the method of making the improved fibers and separatory cells such as hemodialyzers or hemofilters which contain the improved fibers in a gamma ray sterilized condition.
Inventors
- 👤 David T. Chen
- 👤 Robert D. Mahoney
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 19:42
CPC Classifications
B; B01; B01D; B01D71/00; B01D71/06; B01D71/08; B01D71/10; B01D69/00; B01D69/08; D; D01; D01D; D01D5/00; D01D5/24
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
170 words
A process for making a semipermeable cellulose hollow fiber having an ultrafiltration coefficient K UFR in the range of about 2 to about 200 milliliters per hour per square meter per millimeter of mercury, a urea coefficient K UREA in the range of about 15×10 -3 to about 45×10 -3 centimeters per minute, and a wet intrinsic tensile strength in the range of about 2×10 4 to about 11×10 4 force per gram of cellulose polymer which comprises: (a) melt spinning a hollow fiber cellulose ester fiber through a nozzle from a melt spin composition consisting essentially of about 36 to less than 50 weight percent cellulose ester and the balance at least one polyol having an average molecular weight between about 106 and about 900; (b) hydrolyzing said cellulose ester fiber with an aqueous alkali solution free of glycerol, substantially into a cellulose hollow fiber; (c) replasticizing said cellulose fiber while said fiber is still wet with a water soluble, essentially non-volatile plasticizer; and (d) drying said plasticizer fiber.
Claim 2
Dependent Claim
170 words
A process for making a semipermeable cellulose hollow fiber having an ultrafiltration coefficient K UFR in the range of about 2 to about 200 milliliters per hour per square meter per millimeter of mercury, a urea coefficient K UREA in the range of about 15×10 -3 to about 45×10 -3 centimeters per minute, and a wet intrinsic tensile strength in the range of about 2×10 4 to about 11×10 4 force per gram of cellulose polymer which comprises: (a) melt spinning a hollow fiber cellulose ester fiber through a nozzle from a melt spin composition consisting essentially of about 36 to less than 50 weight percent cellulose ester and the balance at least one polyol having an average molecular weight between about 106 and about 900; (b) hydrolyzing said cellulose ester fiber with an aqueous alkali solution free of glycerol, substantially into a cellulose hollow fiber; (c) replasticizing said cellulose fiber while said fiber is still wet with a water soluble, essentially non-volatile plasticizer; and (d) drying said plasticizer fiber.
Claim 3
Dependent Claim
21 words
A process in accordance with claim 1 wherein said melt spin composition contains about 36 to about 43 percent cellulose ester.
Claim 4
Dependent Claim
15 words
A process in accordance with claim 1 wherein said ester consists essentially of cellulose diacetate.
Claim 5
Dependent Claim
15 words
A process in accordance with claim 1 wherein said cellulose ester includes cellulose acetate propionate.
Claim 6
Dependent Claim
26 words
A process in accordance with claim 1 wherein polyol is at least one polyol selected from the group consisting of polyethylene glycols, polypropylene glycols and glycerine.
Claim 7
Dependent Claim
35 words
A process in accordance with claim 1 wherein said melt/spin composition consists essentially of a blend, by weight, of 43% cellulose diacetate and 57% of polyethylene glycol having an average molecular weight of 400 Daltons.
Claim 8
Dependent Claim
48 words
A process in accordance with claim 1 wherein said malt/spin composition consists essentially of a mixture, by weight, of 43% cellulose diacetate and 57%, by weight, of a mixture of polyethylene glycols of molecular weights 400 and 1450 Daltons and having an average molecular weight of 713 Daltons.
Claim 9
Dependent Claim
55 words
A process in accordance with claim 1 wherein said melt/spin composition consists essentially of a blend, by weight, of 43% cellulose diacetate and 57% of a mixture of polyethylene glycol of molecular weight 400 Daltons and glycerine of molecular weight 92 Daltons to give a polyol blend having an average molecular weight of 362 Daltons.
Claim 10
Dependent Claim
53 words
A process in accordance with claim 1 wherein said melt/spin composition consists essentially of a blend, by weight, of 36% cellulose diacetate and 64% of a polyol blend of polyethylene glycol having an average molecular weight of 600 Daltons and glycerine in an amount to produce an average molecular weight of 421 Daltons.
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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) | 1988-09-23 | 1989-03-25 | 1989-09-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-09-23 | 1993-03-25 | 1993-09-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-09-23 | 1997-03-25 | 1997-09-24 | $7700.00 | Window Closed / Lapsed |