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A kind of high molecular weight polytetrafluoroethylene dispersed resin and preparation method thereof

A polytetrafluoroethylene and dispersing resin technology, applied in the chemical industry, can solve the problems of general resin molecular weight level, difficult to meet the high-strength large-scale product processing equipment, etc., and achieve the effects of uniform appearance, not easy to break, and good air permeability

Active Publication Date: 2020-07-14
ZHONGHAO CHENGUANG RES INST OF CHEMICALINDUSTRY CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The molecular weight level of the resin in this patent is average, and it is difficult to meet the needs of high-strength large-scale product processing equipment

Method used

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  • A kind of high molecular weight polytetrafluoroethylene dispersed resin and preparation method thereof
  • A kind of high molecular weight polytetrafluoroethylene dispersed resin and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] Clean the 50L stainless steel reaction kettle, add 32L of deionized water, 0.15g of potassium bromate, 2g of succinic acid, 8g of perfluorooctanoic acid ammonium, and 2kg of paraffin. content, when the oxygen content is less than or equal to 30ppm, it is qualified. After the oxygen analysis is qualified, 5 g of perfluorobutylethylene (modifier) ​​is added through a metering pump. The temperature of the reaction kettle is raised to 70±1°C, and the gas-phase monomer tetrafluoroethylene is put into the kettle until the pressure inside the kettle is 2.5MPa, and 0.1g of sodium sulfite (reducing initiator) is added through a metering pump (diluted with 2L of deionized water), and another metering The pump continuously drips sodium sulfite with a concentration of 0.5g / L, and a total of 0.6g is added dropwise. During the reaction, the pressure in the kettle was maintained at 2.5MPa, and the temperature was 70-75°C. According to the change of the polymerization reaction speed,...

Embodiment 2

[0035] Clean the 50L stainless steel reaction kettle, add 32L of deionized water, 0.15g of potassium bromate, 2g of succinic acid, 8g of perfluorooctanoic acid ammonium, and 2kg of paraffin. content, when the oxygen content is less than or equal to 30ppm, it is qualified. After passing the oxygen analysis, 2.5 g of perfluorobutylethylene (modifier) ​​was added through a metering pump. The temperature of the reaction kettle is raised to 70±1°C, and the gas-phase monomer tetrafluoroethylene is put into the kettle until the pressure inside the kettle is 2.5MPa, and 0.1g of sodium sulfite (reducing initiator) is added through a metering pump (diluted with 2L of deionized water), and another metering The pump continuously drips sodium sulfite with a concentration of 0.5g / L, and a total of 0.6g is added dropwise. During the reaction, the pressure in the kettle was maintained at 2.5MPa, and the temperature was 70-75°C. According to the change of the polymerization reaction speed, t...

Embodiment 3

[0037]Clean the 50L stainless steel reaction kettle, add 32L of deionized water, 0.15g of potassium bromate, 2g of succinic acid, 8g of perfluorooctanoic acid ammonium, and 2kg of paraffin. content, when the oxygen content is less than or equal to 30ppm, it is qualified. After the oxygen analysis is qualified, 1 g of perfluorobutylethylene (modifier) ​​is added through a metering pump. The temperature of the reaction kettle is raised to 70±1°C, and the gas-phase monomer tetrafluoroethylene is put into the kettle until the pressure inside the kettle is 2.5MPa, and 0.1g of sodium sulfite (reducing initiator) is added through a metering pump (diluted with 2L of deionized water), and another metering The pump continuously drips sodium sulfite with a concentration of 0.5g / L, and a total of 0.6g is added dropwise. During the reaction, the pressure in the kettle was maintained at 2.5MPa, and the temperature was 70-75°C. According to the change of the polymerization reaction speed, ...

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Abstract

The invention specifically relates to a high-molecular-weight polytetrafluoroethylene dispersion resin and a preparation method thereof, belonging to the field of the chemical industry. The preparation method comprises the following steps: adding a stabilizer, a dispersant, an anti-sticking agent, etc. into an aqueous medium; and adding tetrafluoroethene monomers and carrying out dispersion and polymerization under the action of a modifier at a certain temperature and a certain pressure via an oxidation-reduction initiating system to prepare the polytetrafluoroethylene dispersion resin with SSG of 2.14 to 2.15. The polytetrafluoroethylene dispersion resin obtained in the invention is high in molecular weight and narrow and uniform in molecular weight distribution; when used for spinning, the polytetrafluoroethylene dispersion resin is high in filament formation rate and not prone to filament breakage; and he polytetrafluoroethylene dispersion resin has the characteristics of high membrane strength, uniform appearance, good air permeability and the like when used for preparing a microporous membrane.

Description

technical field [0001] The invention relates to the field of chemical industry, in particular to a high molecular weight polytetrafluoroethylene dispersion resin and a preparation method thereof. Background technique [0002] The excellent chemical corrosion resistance, high and low temperature resistance, aging resistance, low friction, non-stickiness, and physiological inertia of PTFE make it an indispensable special material in the fields of chemical industry, machinery, electrical, construction, and medical treatment. , it can be used for a long time in the temperature range of -250 ~ 250 ℃. With the advancement of dispersion resin molding and processing technology and the expansion of the application range of PTFE resin, the quality of extruded PTFE dispersion resin has been improved and developed to high-end. High-molecular-weight polytetrafluoroethylene dispersion resin has high molecular weight and narrow molecular weight distribution. It can be used to process and ...

Claims

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Application Information

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IPC IPC(8): C08F214/26C08F214/18C08F4/40
CPCC08F4/40C08F214/182C08F214/26
Inventor 苏小龙张建新胡显权姚权卫张春静罗湘华
Owner ZHONGHAO CHENGUANG RES INST OF CHEMICALINDUSTRY CO LTD