US4444716A
Expired / Lapsed
US
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Method for manufacture of hollow fiber
Assignee: Terumo Corp
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Filing: 1982-05-25
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Granted: 1984-04-24
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Expires: 2002-05-25
Abstract
Abstract A method for the manufacture of a hollow fiber which comprises extruding a cellulosic spinning dope through an annular spinning nozzle directly into a non-coagulative liquid layer in a bath filled in the upper layer with a coagulative liquid relative to said spinning dope and in the lower layer with a non-coagulative liquid of a halogenated hydrocarbon and, at the same time, introducing a non-coagulative liquid relative to said spinning dope into the inner center of the tubularly extruded thread of spinning dope, and subsequently passing the resultant tubular fiber of spinning dope through said coagulative liquid thereby coagulating and regenerating the fiber.
Inventors
- 👤 Juuro Aoyagi
- 👤 Kazuaki Takahara
- 👤 Yukio Seita
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 11:53
CPC Classifications
B; B01; B01D; B01D71/00; B01D71/06; B01D71/08; B01D71/10; B01D69/00; B01D69/08; B01D69/087; D; D01; D01D; D01D5/00; D01D5/24; D01F; D01F2/00; D01F2/02; D01F2/04; B01D2323/00; B01D2323/42
Claims Analysis
Total Claims: 22
Claim 1
Independent Claim
154 words
A method of producing a hollow fiber having a substantially circular cross-section, said method comprising: (a) extruding a metal ammonia cellulose containing spinning dope through an annular spinning nozzle directly into a lower layer of a two-layer bath, said lower layer containing a first non-coagulating liquid selected from the group consisting of halogenated hydrocarbons and said bath further comprising an upper layer containing a coagulating liquid to thereby form a tubular extruded thread, wherein the height of the first non-coagulating liquid of the lower layer measured from the annular spinning nozzle to the interface of the first non-coagulating liquid and the upper layer is between 50 and 250 mm, and simultaneously introducing into the tubular hollow of said tubular extruded thread a second non-coagulating liquid; and (b) passing said tubular extruded thread containing said second non-coagulating liquid upwardly into and through said upper layer containing said coagulating liquid to thereby form said hollow fiber.
Claim 2
Independent Claim
154 words
A method of producing a hollow fiber having a substantially circular cross-section, said method comprising: (a) extruding a metal ammonia cellulose containing spinning dope through an annular spinning nozzle directly into a lower layer of a two-layer bath, said lower layer containing a first non-coagulating liquid selected from the group consisting of halogenated hydrocarbons and said bath further comprising an upper layer containing a coagulating liquid to thereby form a tubular extruded thread, wherein the height of the first non-coagulating liquid of the lower layer measured from the annular spinning nozzle to the interface of the first non-coagulating liquid and the upper layer is between 50 and 250 mm, and simultaneously introducing into the tubular hollow of said tubular extruded thread a second non-coagulating liquid; and (b) passing said tubular extruded thread containing said second non-coagulating liquid upwardly into and through said upper layer containing said coagulating liquid to thereby form said hollow fiber.
Claim 3
Dependent Claim
13 words
The method of claim 1, wherein said metal ammonia cellulose is cuprammonium cellulose.
Claim 4
Dependent Claim
52 words
The method of claim 1, wherein the spinning dope further comprises a permeability regulating agent selected from ammonium and alkali metal salts of a polymer or copolymer having a number average molecular weight of between 500 and 200,000, said polymer or copolymer containing 10 to 70 equivalent percent of a carboxyl group.
Claim 5
Dependent Claim
26 words
The method of claim 1, wherein the specific gravity of the tubular extruded thread containing said second non-coagulating liquid is less than said first non-coagulating liquid.
Claim 6
Dependent Claim
18 words
The method of claim 4, wherein the specific gravity of said first non-coagulating liquid is at least 1.3.
Claim 7
Dependent Claim
24 words
The method of claim 4, wherein the specific gravity of said tubular extruded thread containing said second non-coagulating agent is between 1.05 and 1.15.
Claim 8
Dependent Claim
19 words
The method of claim 5, wherein the specific gravity of the first non-coagulating liquid is between 1.4 and 1.7.
Claim 9
Dependent Claim
28 words
The method of claim 5, wherein the first non-coagulating liquid is selected from those having a solubility in water of up to 0.05 g/100 ml at 21° C.
Claim 10
Dependent Claim
16 words
The method of claim 1, wherein said first non-coagulating liquid is selected from tetrachloroethylene and trichlorotrifluoroethane.
Claim 11
Dependent Claim
19 words
The method of claim 4, wherein the specific gravity of said second non-coagulating liquid is between 0.65 and 1.00.
Claim 12
Dependent Claim
35 words
The method of claim 4, wherein said second non-coagulating liquid is selected from the group consisting of n-hexane, n-heptane, n-octane, n-decane, n-dodecane, liquid paraffin, isopropyl myristate, light oil, kerosene, benzene, toluene, xylene, styrene, and ethylbenzene.
Claim 13
Dependent Claim
14 words
The method of claim 1, wherein the coagulating liquid is an aqueous alkali solution.
Claim 14
Dependent Claim
23 words
The method of claim 12, wherein the aqueous alkali solution is a sodium hydroxide solution having a concentration of 30 to 150 g/liter.
Claim 15
Dependent Claim
18 words
The method of claim 13, wherein the concentration of the sodium hydroxide solution is 35 to 80 g/liter.
Claim 16
Dependent Claim
30 words
The method of claim 1, wherein the fiber hollow has a diameter of between 50 and 500 μm and the thickness of the wall is between 5 and 60 μm.
Claim 17
Dependent Claim
30 words
The method of claim 15, wherein the ratio of the minimum thickness of the wall and the maximum thickness of the wall is in the range of 0.2:1 to 0.8:1.
Claim 18
Dependent Claim
23 words
The method of claim 1, wherein the rate of extrusion of the dope through the annular spinning nozzle is at least 30 m/min.
Claim 19
Dependent Claim
23 words
The method of claim 17, wherein the rate of extrusion of the dope through the annular spinning nozzle is at least 38 m/min.
Claim 20
Independent Claim
184 words
A method of producing a hollow fiber having a substantially circular cross-section having a diameter of between 50 and 500 μm, said method comprising: (a) extruding a metal ammonia cellulose containing spinning dope through an annular spinning nozzle directly into a lower layer of a two-layer bath, said lower layer containing a first non-coagulating liquid having a specific gravity of at least 1.3 and selected from the group consisting of halogenated hydrocarbons, and said bath further comprising an upper layer containing a sodium hydroxide solution having a concentration of between 30 and 150 g/liter, wherein the height of the first non-coagulating liquid of the lower layer measured from the annular spinning nozzle to the interface of the non-coagulating liquid and the upper layer is between 50 and 250 mm, and simultaneously introducing into the tubular hollow of said tubular extruded thread a second non-coagulating liquid having a specific gravity of between 0.65 and 1.0; and (b) passing said tubular extruded thread containing said second non-coagulating liquid upwardly into and through said upper layer containing said sodium hydroxide solution to thereby form said hollow fiber.
Claim 21
Independent Claim
184 words
A method of producing a hollow fiber having a substantially circular cross-section having a diameter of between 50 and 500 μm, said method comprising: (a) extruding a metal ammonia cellulose containing spinning dope through an annular spinning nozzle directly into a lower layer of a two-layer bath, said lower layer containing a first non-coagulating liquid having a specific gravity of at least 1.3 and selected from the group consisting of halogenated hydrocarbons, and said bath further comprising an upper layer containing a sodium hydroxide solution having a concentration of between 30 and 150 g/liter, wherein the height of the first non-coagulating liquid of the lower layer measured from the annular spinning nozzle to the interface of the non-coagulating liquid and the upper layer is between 50 and 250 mm, and simultaneously introducing into the tubular hollow of said tubular extruded thread a second non-coagulating liquid having a specific gravity of between 0.65 and 1.0; and (b) passing said tubular extruded thread containing said second non-coagulating liquid upwardly into and through said upper layer containing said sodium hydroxide solution to thereby form said hollow fiber.
Claim 22
Dependent Claim
13 words
The method of claim 19, wherein said metal ammonia cellulose is cuprammonium cellulose.
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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) | 1987-04-24 | 1987-10-24 | 1988-04-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-04-24 | 1991-10-24 | 1992-04-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-04-24 | 1995-10-24 | 1996-04-24 | $7700.00 | Window Closed / Lapsed |