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Method for preparing fluorine-containing polymer by dispersion process

A technology of polymer and dispersion method, applied in the field of fluorine chemical industry, can solve the problems of high toxicity, can not fully meet the requirements of environmental friendliness, poor dispersibility, etc., and achieve the effect of low toxicity

Active Publication Date: 2014-12-24
SHANDONG DONGYUE POLYMER MATERIAL
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

For example: Chenguang Chemical Industry Research Institute mentioned in Chinese patent document CN101648122A (application number 200910092202.2) that fluorine-containing olefins were oxidized by oxygen at low temperature to prepare ether-containing surfactants. The surfactants obtained by this method contained a large amount of Branched chain, poor dispersion during polymerization
In the Chinese patent document CN102504063A (Application No. 201110338501), Juhua Group uses a surfactant with a fluorine-containing ether segment containing chlorine atoms. This surfactant is highly toxic and cannot fully meet the requirements of environmental friendliness.
The surfactants mentioned in U.S. Patent Nos. 5,789,508, 4,025,709, 5,688,884, and 5,763,552, etc., will affect the product quality of the polymer during the polymerization process due to the relationship between the molecular structure

Method used

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Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0039] Preparation of emulsifier:

[0040] C 4 f 9 -CH 2 -CF 2 Synthesis of -COOH

[0041] (i) Preparation C 4 f 9 -CH 2 -CF 2 -CH 2 -CF 2 I

[0042] Add 173g (Mw=346, 0.5M) C into a 1L autoclave 4 f 9 I. Cool to -78°C, add 52g CF after evacuating the reactor 2 =CH 2 . The mixture was heated to 210°C for 15 hours, and then the unreacted C was separated by rectification. 4 f 9 I and C 4 f 9 I and CF 2 =CH 2 Different proportions of adducts are collected by rectification at 25mmHg pressure and the temperature at the top of the tower is 82-84°C. 4 f 9 I and CF 2 =CH 2 A total of 47.0 g of the product obtained by addition of 1:2 was collected.

[0043] (ii) Preparation C 4 f 9 -CH 2 -CF 2 -CH=CF 2

[0044] will contain 82g C 4 f 9 -CH 2 -CF 2 -CH 2 -CF 2 A mixture of I and 11.0g LiCl was added to 90mL of dimethylformamide, slowly heated to 150°C, kept at a pressure of 150-200mmHg for 3.5 hours, and then cooled to -10°C. The material is separa...

Embodiment 1

[0050] Add 1400Kg deionized water and 2.1kg emulsifier C to the 2000L horizontal stainless steel polymerization kettle 4 f 9 -CH 2 -CF 2 -COONH 4 , 1000g succinic acid (pH regulator) and 60kg solid paraffin. At 65°C, the polymerization vessel was evacuated and replaced three times with tetrafluoroethylene (TFE). The stirring speed was 45 rpm, and the pressure was raised to 2.7 MPa with tetrafluoroethylene, and 1.0 g of ammonium persulfate (APS) was dissolved in 1000 ml of deionized water, and added at a speed of 100 ml / min. After the addition, use tetrafluoroethylene (TFE) to maintain the pressure at 2.7MPa. The reaction was completed after supplying 480 kg of tetrafluoroethylene (TFE). The reaction time is 2.3 hours, the mass concentration of fluoropolymer in the emulsion is 25.1%, and the average primary particle size is 253nm. After the reaction, no coagulation was produced. The dispersion was coagulated, washed with water and dried to obtain 470kg of powder. Parti...

Embodiment 2

[0052] Add 1400Kg deionized water and 2.3kg emulsifier C to the 2000L horizontal stainless steel polymerization kettle 4 f 9 -CH 2 -CF 2 -COONH 4 , 850g succinic acid and 70kg solid paraffin. At 70°C, the polymerization vessel was evacuated and replaced three times with tetrafluoroethylene (TFE). The stirring speed is 45rpm, 1.5kg of hexafluoropropylene is added, and the pressure is increased to 2.5MPa with tetrafluoroethylene, 1.2g of ammonium persulfate (APS) is dissolved in 1000ml of deionized water, and added at a speed of 100ml / min. After the addition, use tetrafluoroethylene (TFE) to maintain the pressure at 2.5MPa. The reaction was completed after supplying 500 kg of tetrafluoroethylene (TFE). The reaction time is 3.2 hours, the mass concentration of fluoropolymer in the emulsion is 26.2%, and the average primary particle size is 270nm. After the reaction, no coagulation was produced. The dispersion was coagulated, washed with water and dried to obtain 490kg of ...

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Abstract

The invention relates to a method for preparing a fluorine-containing polymer by a dispersion process, which comprises the following steps: carrying out polymerization reaction on a fluorine-containing monomer in the presence of an emulsifier and an initiator in a water phase system at 50-150 DEG C under the reaction pressure of 0.3-7 MPa, and after the reaction finishes, carrying out aggregation separation, water washing and drying on the fluorine-containing polymer in the reaction emulsion to obtain the solid fluorine-containing polymer; or concentrating the reaction emulsion until the concentration of the fluorine-containing polymer in the concentrated solution is 30-70 wt% to obtain the fluorine-containing polymer concentrated solution, wherein the emulsifier accounts for 0.01-2.0 wt% of the water in the reaction system in the polymerization process. By adopting the emulsifier, the fluorine-containing polymer, which has excellent properties and lower toxicity than the prior art, can be obtained, and the service performance and biological toxicity have the optimal balance.

Description

technical field [0001] The invention relates to a method for preparing a fluorine-containing polymer by a dispersion method, and belongs to the technical field of fluorine chemical industry. Background technique [0002] The most widely used fluorosurfactant in the field of dispersion production of fluoropolymers is perfluorooctanoic acid, namely C 7 f 15 COOH and its derivatives, or "C8", are synthetic rather than naturally occurring industrial raw materials. While the molecular structure of PFOA endows it with excellent surface properties, it is also doomed to its persistence and accumulation in the environment. Because PFOA molecules contain perfluorinated groups and the carbon chains connected to each other are relatively long, PFOA has strong thermal stability and dynamic stability, which increases the persistence of PFOA molecules in the environment. Studies have shown that PFOA is difficult to degrade under strong heat, light, chemical action, microbial action and ...

Claims

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Application Information

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IPC IPC(8): C08F114/26C08F214/26C08F214/28C08F214/24C08F2/24
Inventor 夏俊张宝亮马鹏飞魏文涛
Owner SHANDONG DONGYUE POLYMER MATERIAL
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