CN103184543A - Production method of nylon-66 high-strength yarn - Google Patents
Production method of nylon-66 high-strength yarn Download PDFInfo
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- CN103184543A CN103184543A CN 201110451807 CN201110451807A CN103184543A CN 103184543 A CN103184543 A CN 103184543A CN 201110451807 CN201110451807 CN 201110451807 CN 201110451807 A CN201110451807 A CN 201110451807A CN 103184543 A CN103184543 A CN 103184543A
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Abstract
The invention provides a production method of a nylon-66 high-strength yarn. The production method comprises the following step of: processing a nylon-66 saline solution, which is taken as a raw material, by a concentration tank, a reactor, a pressure reducer, a front polymerizer, a back polymerizer, a spinning yarn conveying pump, a spinning box used for spinning, a draw machine used for drawing and a winding machine used for winding in sequence, wherein the mass concentration of the concentration tank is 770g/L; the temperature of the reactor is 255 DEG C; the temperature of the spinning box is 313 DEG C; and the draw ratio is 5.54. The production method of the nylon-66 high-strength yarn, disclosed by the invention, has the following technical effect that a produced nylon-66 high-strength yarn product is stable in quality, fewer in fuzziness and yarn breakage phenomena, good in spinnability and low in production cost.
Description
Technical field
The present invention relates to a kind of production method of polyamide fibre 66 high strength yarns, belong to the chemical fibre technical field.
Background technology
Polyamide fibre 66 high strength yarns are the very big chemical fibre raw materials of a kind of market potential, have intensity height, fatigue durability is good, DIMENSIONAL STABILITY is good, dry-hot shrinkage is low advantage, can be used as the framework material of tire.
The polyamide fibre 66 high strength yarn unstable product quality that the production method of existing polyamide fibre 66 high strength yarns is produced, indexs such as intensity, percentage elongation, dry-hot shrinkage are undesirable.
Summary of the invention
The objective of the invention is to overcome the deficiencies in the prior art part, a kind of production method of polyamide fibre 66 high strength yarns is provided.
The production method of polyamide fibre 66 high strength yarns of the present invention, may further comprise the steps: be raw material with polyamide fibre 66 saline solutions, process thickener, reactor, pressure reducer, pre-polymerization device, back polymerizer, spinning delivery pump, manifold are carried out spinning successively, drawing machine carries out drawing-off and up-coiler is reeled
Said thickener mass concentration is 770g/L.
Said temperature of reactor is 255 degrees centigrade.
Said condition of spinning manifold temperature is 313 degrees centigrade.
Said draw ratio is 5.54.
The production method of polyamide fibre 66 high strength yarns of the present invention has following technique effect: the polyamide fibre 66 high strength yarn constant product quality of producing, and lousiness and fracture of wire phenomenon are less, good spinnability, production cost is low.
The specific embodiment
Embodiment 1
The production method of polyamide fibre 66 high strength yarns of present embodiment, may further comprise the steps: be raw material with polyamide fibre 66 saline solutions, process thickener, reactor, pressure reducer, pre-polymerization device, back polymerizer, spinning delivery pump, manifold are carried out spinning successively, drawing machine carries out drawing-off and up-coiler is reeled, and the thickener mass concentration is 770g/L.Temperature of reactor is 255 degrees centigrade.Condition of spinning manifold temperature is 313 degrees centigrade.Draw ratio is 5.54.
Claims (1)
1. the production method of polyamide fibre 66 high strength yarns, may further comprise the steps: be raw material with polyamide fibre 66 saline solutions, process thickener, reactor, pressure reducer, pre-polymerization device, back polymerizer, spinning delivery pump, manifold are carried out spinning successively, drawing machine carries out drawing-off and up-coiler is reeled
It is characterized in that,
Said thickener mass concentration is 770g/L;
Said temperature of reactor is 255 degrees centigrade;
Said condition of spinning manifold temperature is 313 degrees centigrade;
Said draw ratio is 5.54.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN 201110451807 CN103184543A (en) | 2011-12-30 | 2011-12-30 | Production method of nylon-66 high-strength yarn |
Applications Claiming Priority (1)
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CN 201110451807 CN103184543A (en) | 2011-12-30 | 2011-12-30 | Production method of nylon-66 high-strength yarn |
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CN103184543A true CN103184543A (en) | 2013-07-03 |
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CN 201110451807 Pending CN103184543A (en) | 2011-12-30 | 2011-12-30 | Production method of nylon-66 high-strength yarn |
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CN (1) | CN103184543A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106811818A (en) * | 2016-12-30 | 2017-06-09 | 神马实业股份有限公司 | A kind of high drawing abnormity 66 nylon fiber and its production method |
CN111363142A (en) * | 2020-04-27 | 2020-07-03 | 扬州惠通化工科技股份有限公司 | High-capacity nylon polymerization system |
-
2011
- 2011-12-30 CN CN 201110451807 patent/CN103184543A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106811818A (en) * | 2016-12-30 | 2017-06-09 | 神马实业股份有限公司 | A kind of high drawing abnormity 66 nylon fiber and its production method |
CN106811818B (en) * | 2016-12-30 | 2018-11-20 | 神马实业股份有限公司 | A kind of high drawing abnormity 66 nylon fiber and its production method |
CN111363142A (en) * | 2020-04-27 | 2020-07-03 | 扬州惠通化工科技股份有限公司 | High-capacity nylon polymerization system |
CN111363142B (en) * | 2020-04-27 | 2021-03-19 | 扬州惠通科技股份有限公司 | High-capacity nylon polymerization system |
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PB01 | Publication | ||
C05 | Deemed withdrawal (patent law before 1993) | ||
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Application publication date: 20130703 |