US4624816A
Expired / Lapsed
US
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Process for the manufacture of polyamide fibers
Assignee: Toyobo Co Ltd
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Filing: 1984-05-31
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Granted: 1986-11-25
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Expires: 2004-05-31
Abstract
Abstract A process for the manufacture of polyamide fibers including melt spinning a polyamide having a relative viscosity of not less than 3.50 under conditions satisfying the following relationships: Q/D.sup.3 ≦982 g/sec.cm.sup.3 D.sup.2.Vw/Q≦12.8 cm.sup.3 /g T.sub.20 ≧100° C. Δn of unstretched filaments≦0.017 The resultant filaments are then subjected to cooling, stretching and heat treatment resulting in fibers with a break strength of not less than 11.0 g/d, a break strength×(break elongation(%))1/2 of not less than 46.0 and a monofilament denier of not more than 60 d.
Inventors
- 👤 Kazuo Kurita
- 👤 Hideaki Ishihara
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 20:03
CPC Classifications
D; D01; D01F; D01F6/00; D01F6/58; D01F6/60; D01D; D01D5/00; D01D5/12; D01D5/16; Y; Y10; Y10S; Y10S260/00; Y10S260/23; Y10T; Y10T428/00; Y10T428/29; Y10T428/2913
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
203 words
A process for the manufacture of polyamide fibers which comprises the steps of: melt spinning a polyamide having a relative viscosity of not less than 3.50 under the conditions satisfying the following relationships: Q/D 3 ≦982 g/sec.cm 3 D 2 .Vw/Q≦12.8 cm 3 /g T 20 ≧100° C. Δn of unstretched filament≦0.017 (wherein Q is the discharge amount per each nozzle hole (g/sec); D is the diameter of each nozzle hole (cmφ), Vw is the take up speed of spun filaments (cm/sec) T 20 is the atmospheric temperature at a distance of 5 mm from the spun filaments and at a distance of 20 mm from the nozzle face towards the discharge of the filaments (°C.) and Δn of the unstretched filaments is the value determined after the filaments are allowed to stand at a temperature of 30° C. under a relative humidity of 80% for a period of 24 hours); subjecting the resultant filaments to cooling; further subjecting the resulting filaments to stretching and heat treatment; and providing said fibers with a break strength of not less than 11.0 g/d, said break strength (g/d)×(the break elongation (%)) 1/2 being not less than 46.0, and a monofilament denier of not more than 60d.
Claim 2
Dependent Claim
203 words
A process for the manufacture of polyamide fibers which comprises the steps of: melt spinning a polyamide having a relative viscosity of not less than 3.50 under the conditions satisfying the following relationships: Q/D 3 ≦982 g/sec.cm 3 D 2 .Vw/Q≦12.8 cm 3 /g T 20 ≧100° C. Δn of unstretched filament≦0.017 (wherein Q is the discharge amount per each nozzle hole (g/sec); D is the diameter of each nozzle hole (cmφ), Vw is the take up speed of spun filaments (cm/sec) T 20 is the atmospheric temperature at a distance of 5 mm from the spun filaments and at a distance of 20 mm from the nozzle face towards the discharge of the filaments (°C.) and Δn of the unstretched filaments is the value determined after the filaments are allowed to stand at a temperature of 30° C. under a relative humidity of 80% for a period of 24 hours); subjecting the resultant filaments to cooling; further subjecting the resulting filaments to stretching and heat treatment; and providing said fibers with a break strength of not less than 11.0 g/d, said break strength (g/d)×(the break elongation (%)) 1/2 being not less than 46.0, and a monofilament denier of not more than 60d.
Claim 3
Dependent Claim
23 words
The process according to claim 1, wherein after cooling the filaments are taken up and then subjected to said stretching and heat treatment.
Claim 4
Dependent Claim
32 words
The process according to claim 1, wherein the polyamide fiber comprises polycapramide in an amount of not less than 75% by weight on the basis of the weight of the polyamide fiber.
Claim 5
Dependent Claim
52 words
The process according to claim 1, wherein the spinning is carried out at an atmospheric temperature of not lower than 100° C., the temperature being measured at a distance of 5 mm from the filaments and at a distance of 300 mm from the nozzle surface towards the discharge of the filament.
Claim 6
Dependent Claim
84 words
The process according to claim 1, wherein the polyamide has a relative viscosity of not less than 4.0 and the spinning is carried out under the conditions satisfying the following relationships: Q/D 3 ≦500 g/sec.cm 3 D 2 .Vw/Q≦5.0 cm 3 /g T 300 ≧100° C. Δn of unstretched filament≦0.013 (wherein T 300 is the atmospheric temperature at a distance of 5 mm from the spun filaments and at a distance of 300 mm from the nozzle surface towards the discharge of filaments (°C.)).
Claim 7
Dependent Claim
109 words
The process according to claim 1, wherein the stretching and heat treatment is carried out by prestretching the filaments between a 1st feed roller and a 2nd feed roller, said rollers being kept at a temperature below 100° C., to make a stretch ratio of not more than 1.10, subjecting the resulting filaments to 1st stage stretching between the 2nd feed roller and a 1st stretch roller to make a stretch ratio of not less than 50% of the entire stretch ratio, and subjecting the resultant filaments to 2nd stage stretching at a temperature of 100° to 200° C. between the 1st stretch roller and a 2nd stretch roller.
Claim 8
Dependent Claim
96 words
The process according to claim 1, wherein the stretching and heat treatment is carried out by prestretching the filaments between a 1st feed roller and a 2nd feed roller, said rollers being kept at a temperature below 100° C., to make a stretch ratio of not more than 1.10, subjecting the resulting filaments to 1st stage stretching between the 2nd feed roller and a 1st stretch roller to make a stretch ratio of not less than 50% of the entire stretch ratio and subjecting the resultant filaments to further stretching in not less than two steps.
Claim 9
Dependent Claim
74 words
The process according to claim 7, wherein the further stretching is carried out by subjecting the filaments to 2nd stage stretching at a temperature of 100° to 200° C. between the 1st stretch roller and the 2nd stretch roller and subjecting the filaments to 3rd stage stretching at a temperature of 160° to 220° C. and higher than the temperature for 2nd stage stretching between the 2nd stretch roller and the 3rd stretch roller.
Claim 10
Dependent Claim
97 words
The process according to claim 1, wherein the stretching and heat treatment is carried out by prestretching the filaments between a 1st feed roller and a 2nd feed roller, said rollers being kept at a temperature below 100° C., to make a stretch ratio of not more than 1.10 and subjecting the resulting filaments to 1st stage stretching between the 2nd feed roller and a 1st stretch roller while applying pressurized steam of not less than 200° C. to the filaments so as to fix the first stage stretching point around the ejecting head for the steam.
Claim 11
Dependent Claim
101 words
The process according to claim 1, wherein the stretching and heat treatment step is carried out by subjecting the filaments to stretching in two steps and subjecting the filaments to further stretching, and the further stretching is effected while applying pressurized steam of not less than 200° C. to the filaments between the 2nd stage stretch roller and the 3rd stage stretch roller so as to fix the 3rd stage stretching point around the ejecting head for the steam and then at a temperature of 185° to 220° C. between the 3rd stage stretch roller and the 4th stage stretch roller.
Claim 12
Dependent Claim
147 words
The process according to claim 1, wherein the stretching and heat treatment is carried out by prestretching the filaments between a 1st feed roller and a 2nd feed roller, said rollers being kept at a temperature below 100° C., to make a stretch ratio of not more than 1.10, subjecting the resulting filaments to first stage stretching between the 2nd feed roller and a 1st stretching roller to make a stretch ratio of not less than 50% of the entire stretch ratio, subjecting the resultant filaments to second stage stretching between the 1st stretching roller and a 2nd stretching roller while applying pressurized steam of not lower than 200° C. thereto so as to fix the 2nd stage stretching point around the ejecting head for the steam and subjecting the thus obtained filaments to third stage stretching between the 2nd stretching roller and a 3rd stretching roller.
Claim 13
Dependent Claim
16 words
The process according to claim 1, wherein the entire stretch ratio is not less than 4.5.
Claim 14
Dependent Claim
24 words
The process according to claim 1, further comprising the step of providing the relative viscosity of the starting polyamide to not less than 4.0.
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| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
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| 3.5 Years (Year 4) | 1989-11-24 | 1990-05-26 | 1990-11-25 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-11-24 | 1994-05-26 | 1994-11-25 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-11-24 | 1998-05-26 | 1998-11-25 | $7700.00 | Window Closed / Lapsed |