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Spinning solution continuous solidification device and control method thereof

A control method and spinning solution technology, applied in textiles and papermaking, fiber chemical characteristics, etc., can solve the problems of large radial structure difference of primary fibers, complex production process, poor coagulation effect, etc., and achieve refinement and simple operation. , the effect of low production cost

Pending Publication Date: 2016-03-23
GLOBAL ENERGY INTERCONNECTION RES INST CO LTD +3
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The purpose of the present invention is to overcome the problems of poor coagulation effect of multi-stage sections in the prior art, large differences in the radial structure of primary fibers, high cost and complicated production process, etc., and propose a continuous coagulation device for spinning solution and its control method. Its structure is simple, easy to operate, and can be applied industrially. The present invention adopts one-stage coagulation to adjust the concentration distribution of the solution in the coagulation bath by changing the structure of the coagulation bath and the way the coagulation bath solution enters and exits the material, and regulates the fiber double diffusion process. Coagulation to obtain primary fibers with uniform and dense structure

Method used

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  • Spinning solution continuous solidification device and control method thereof
  • Spinning solution continuous solidification device and control method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0033] Acrylonitrile and itaconic acid are used as comonomers, dimethyl sulfoxide is used as a solvent, and azobisisobutyronitrile is used as an initiator. Free radical polymerization is carried out at 60°C to obtain acrylonitrile-itaconic acid binary copolymerization material, the comonomer ratio is 99:1. Spinning can be carried out after 12 hours of single and degassing, the temperature of the control tunnel is 50°C, the supply volume of the metering pump is 1.5ml / r, the speed of the metering pump is adjusted, and the flow rate of the polymer solution at the spinneret hole is controlled to be 40m / h. The filament stream is ejected through the spinneret and enters the composition of DMSO and H 2 0 in the three-stage coagulation bath, wherein the concentration of DMSO in the first-stage coagulation bath is 75%, and the temperature is 60°C; the concentration of DMSO in the second-stage coagulation bath is 45%, and the temperature is 25°C; , the temperature is 25°C. The coagula...

Embodiment 2

[0036] Change the coagulation bath to a continuous coagulation device. The DMSO concentrations of the two feed ports along the fiber running direction of the coagulation bath are 75% and 15% respectively, and the temperatures are 60°C and 25°C respectively. The flow rate is adjusted to ensure that the concentration gradient in the coagulation bath is relatively Constant, the speed of the magnetic stirrer is 600r / min, the temperature of the circulating water in the four temperature-controlled water pipes is 60°C, 50°C, 30°C, and 25°C respectively, the total coagulation time is controlled for 14s, the flow rate of the coagulation bath inlet is 30L / h, and the flow rate of the outlet is 30L / h. The flow rate is 60L / h. All the other process parameters and steps are the same as in Example 1.

Embodiment 3

[0038] Change the coagulation bath to a continuous coagulation device. The DMSO concentrations of the two feed ports along the fiber running direction of the coagulation bath are 75% and 15% respectively, and the temperatures are 60°C and 25°C respectively. The flow rate is adjusted to ensure that the concentration gradient in the coagulation bath is relatively Constant, the rotating speed of the magnetic stirrer is 800r / min, the circulating water temperature in the four temperature-controlled water pipes is 60°C, 50°C, 30°C, and 25°C respectively, and the total solidification time is controlled at 14s. The remaining process parameters and steps are the same as in Example 2.

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Abstract

The invention provides a spinning solution continuous solidification device and a control method thereof. A solidification process is carried out in the same section of a solidification bath groove; by changing the flow of materials of an inlet and an outlet of a solidification bath, the temperature of a temperature control water pipe in the solidification bath and a stirring speed of a magnetic stirrer, the concentration of the solidification bath in the groove is controlled to have gradient distribution and is rapidly balanced; a solidification bath solution in the groove can reach the dynamic balance of the concentration through the supplementation of a newly-prepared solution in a solidification bath preparation tank, and the free dispersion of the solution in the groove, and the gradient distribution of the concentration of the solidification bath solution is realized. The spinning solution continuous solidification device has the advantages that continuous solidification of a polyacrylonitrile solution is realized and the concentration of the solidification bath has the gradient distribution; a multi-grade solidification technology is set to be one-grade solidification, so that the refining of equipment is realized and the structure is simple; and the spinning solution continuous solidification device can continuously produce on a production line, is simple to operate and has strong practicability and low production cost.

Description

technical field [0001] The invention relates to a spinning coagulation technology, in particular to a spinning liquid continuous coagulation device and a control method thereof. Background technique [0002] Carbon fiber has many excellent properties such as low density, high specific strength, high specific modulus, high temperature resistance and corrosion resistance, and has been widely used in various fields of aerospace, national defense and civilian industries. According to the classification of raw materials, carbon fiber can be divided into three types: polyacrylonitrile (PAN)-based, asphalt-based and viscose-based. Among them, PAN-based carbon fiber has become a carbon fiber with the fastest development, the highest output, the most varieties and the widest application due to its simple production process, low production cost and excellent mechanical properties. [0003] At present, the PAN precursor spinning process mainly includes wet method and dry-wet method. A...

Claims

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Application Information

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IPC IPC(8): D01F9/32D01F9/21
CPCD01F9/21D01F9/328
Inventor 朱镇陈新何州文兰逢涛刘辉阳武徐樑华李常清
Owner GLOBAL ENERGY INTERCONNECTION RES INST CO LTD
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