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The defoaming method of polyacrylonitrile stock solution

A polyacrylonitrile and defoaming technology, which is applied in the filtration of spinning solution, filament forming treatment, textile and papermaking, etc., can solve the problems of non-uniformity of the original solution, dry knot, gelation, etc., and achieve a small CV value and good technical effect. , the effect of high strength of the original yarn

Active Publication Date: 2017-06-20
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The technical problem to be solved by the present invention is that high temperature and high vacuum degassing in the prior art tends to make the stock solution inhomogeneous, produce gel or even dry out, and provide a new degassing method for polyacrylonitrile stock solution

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0016] A method for defoaming a polyacrylonitrile stock solution, comprising the following steps: starting a heating device, raising the temperature of a defoaming kettle to 55° C., starting a vacuum pump, keeping the vacuum degree of the defoaming kettle at an absolute pressure of 3000 Pa, and dissolving the polyacrylonitrile into a polyacrylonitrile The weight ratio of the acrylonitrile stock solution is 18%, the temperature is 60°C, and the polyacrylonitrile stock solution with a viscosity of 60Pa.s is slowly transported from the degassing kettle to the defoaming kettle for 30 minutes; After the kettle, turn off the vacuum pump, feed nitrogen into the degassing kettle to pressurize to 0.2MPa, and keep it for 28 hours. After the pressure maintaining is completed, start the vacuum pump and keep the vacuum at an absolute pressure of 2000 Pa for vacuum defoaming for 12 hours to obtain the final polyacrylonitrile spinning stock solution. The above-mentioned raw liquid is transpo...

Embodiment 2

[0018] A method for defoaming a polyacrylonitrile stock solution, comprising the following steps: starting a heating device, raising the temperature of a defoaming kettle to 65° C., starting a vacuum pump, keeping the vacuum degree of the defoaming kettle at an absolute pressure of 2000 Pa, and dissolving the polyacrylonitrile into a polyacrylonitrile The weight ratio of the acrylonitrile stock solution is 22%, the temperature is 60°C, and the polyacrylonitrile stock solution with a viscosity of 100Pa.s is slowly transported from the degassing kettle to the defoaming kettle for 50 minutes; After the kettle, turn off the vacuum pump, feed argon into the degassing kettle to pressurize to 0.1MPa, and keep it for 24 hours. After the pressure maintaining is completed, start the vacuum pump and keep the vacuum degree at an absolute pressure of 3000 Pa for vacuum defoaming for 18 hours to obtain the final polyacrylonitrile spinning stock solution. The above-mentioned raw liquid is tr...

Embodiment 3

[0020] A method for defoaming a polyacrylonitrile stock solution, comprising the following steps: starting a heating device, raising the temperature of a defoaming kettle to 60° C., starting a vacuum pump, keeping the vacuum degree of the defoaming kettle at an absolute pressure of 2000 Pa; The weight ratio of the acrylonitrile stock solution is 22%, the temperature is 65°C, and the polyacrylonitrile stock solution with a viscosity of 80Pa.s is slowly transported from the degassing kettle to the defoaming kettle for 20 minutes; After the still, turn off the vacuum pump, feed nitrogen into the degassing kettle to pressurize to 0.3MPa, and keep it for 20 hours. After the pressure holding is completed, start the vacuum pump and keep the vacuum degree at an absolute pressure of 2000 Pa for vacuum defoaming for 18 hours to obtain the final polyacrylonitrile spinning stock solution. The above-mentioned raw liquid is transported to the filter through a metering pump, and after filtra...

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Abstract

The invention relates to a defoaming method for preparing a polyacrylonitrile stock solution, and aims at solving the problems that a stock solution in the prior art is not uniform, and an upper layer easily generates gel, or is even dried and hardened. According to the technical scheme, the defoaming method for preparing the polyacrylonitrile stock solution comprises the following steps: (a) starting a heating device, heating a defoaming kettle, starting a vacuum pump, vacuumizing the defoaming kettle, slowly conveying the polyacrylonitrile stock solution to the defoaming kettle from a demonomerisation kettle while vacuumizing, closing the vacuum pump after the polyacrylonitrile stock solution completely enters the defoaming kettle, introducing gas to the defoaming kettle, pressurizing and defoaming; (b) after pressurizing and defoaming are finished, starting the vacuum pump, vacuumizing the defoaming kettle, defoaming in vacuum, so as to obtain the final polyacrylonitrile stock solution, and the problems are relatively well solved; the defoaming method can be applied to industrial production of a carbon fiber precursor.

Description

technical field [0001] The invention relates to a method for defoaming polyacrylonitrile stock solution. Background technique [0002] Carbon fiber can be obtained by carbonization of polyacrylonitrile fiber, pitch fiber, viscose or phenolic fiber, among which polyacrylonitrile (PAN)-based carbon fiber is the most widely used, the largest amount, the fastest growing, and occupies an absolute position in carbon fiber production. Advantage. In the preparation process of PAN-based carbon fiber precursor, like most other man-made fibers, the removal of air bubbles in the spinning solution is involved. [0003] The solution will generate bubbles during polymerization or transportation; on the other hand, since the polymerization uses azo compounds as initiators, the nitrogen generated during decomposition is also mixed in the original solution to form bubbles. The polyacrylonitrile stock solution used for carbon fiber spinning has a relatively high viscosity, and these bubbles ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): D01D1/10
CPCD01D1/103
Inventor 史纪友沈志刚李磊屠晓萍
Owner CHINA PETROLEUM & CHEM CORP
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