Fusible polyacrylonitrile resin

A technology of polyacrylonitrile resin and crotonitrile, which is applied in the field of macromolecular polymers, can solve the problems of unreported performance and inability to obtain effects.

Inactive Publication Date: 2005-02-16
SINOPEC SHANGHAI PETROCHEMICAL CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Chinese patents 94118175.8 and 94118177.4 proposed methods for preparing melt-processable polyacrylonitrile by copolymerization of methacrylonitrile and acrylonitrile and copolymerization of methacrylonitrile, ethylenically unsaturated monomer and acrylonitrile respectively. The melting torque of the product at 200°C is listed, other properties are not reported in detail
The second comonomer used in the meltable polyacrylonitrile resin produced by the existing chemical modification method fails to solve this problem structurally, so it cannot obtain very ideal effect

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1~7

[0020] Suspension polymerization is carried out with water as the medium in a reactor equipped with a reflux condenser, an electric stirrer and an electric temperature controller. According to the composition in Table 1, the acrylonitrile / butacrylonitrile mixed monomer is dropped into the mode of feed, the monomer feed concentration is 30%, and the add-on of oxidant ammonium persulfate in the initiator is the total amount of oxidant and monomer The weight ratio of the reducing agent sodium metabisulfite is 1: 100, and the weight ratio of the reducing agent to the total amount of monomers is 1: 100. According to the molecular weight required by the product, an appropriate amount of molecular weight regulator isopropanol is added. The reaction temperature was 75°C. After 3 hours, the reaction mixture was filtered, washed, and then dried in a vacuum oven at 80°C for 10 hours to obtain a white powdery polypropylene resin product.

[0021] The viscosity-average molecular weight and...

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PUM

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Abstract

The polyacrylonitrile resin features that the polymer molecule chain contains copolymerized crotononitrile units in 10-15 wt% and the homogeneous copolymerization of acrylonitrile units and crotononitrile units. The polymer has viscosity-average molecular weight of 2000-4000. Crotononitrile used as copolymerized monomer has one more methylene group than acrylonitrile and thus can damage the hexatomic ring structure formed with adjacent acrylonitrile monomer and lower the ring forming probability in the molecular chain. In addition, the two kinds of unsaturated olefine monomer with cyano group have very high compatibility and near reactivity ratio, and this results in the easy control of reaction, fusible polymer for fusion processing and fusion spinning to produce polyacrylonitrile fiber. The addition of the copolymerized component has no influence to the spinning performance and the physical performance of fiber.

Description

technical field [0001] The invention relates to a high molecular polymer, in particular to a high molecular polymer whose polymerization monomer is acrylonitrile. Background technique [0002] Polyacrylonitrile resin is a high polymer with a wide range of uses, especially the fiber performance of polypropylene resin is similar to that of wool, and it occupies a large proportion in the total production of synthetic fibers. However, a defect of polyacrylonitrile resin is that the melting point (theoretical value is 319°C) is higher than the decomposition temperature (generally 250°C), so it cannot be processed by melting, and polyacrylonitrile fibers can usually only be processed by solution spinning. This spinning method uses a large amount of toxic, harmful or corrosive solvents. During the production process, the solvent must be recovered and purified, and the fibers must be washed and dried. Therefore, the process is complicated and the environment is seriously polluted. ...

Claims

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Application Information

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IPC IPC(8): C08F220/44
Inventor李荣安柳帅季春晓
OwnerSINOPEC SHANGHAI PETROCHEMICAL CO LTD