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Polychlorotrifluoroethylene resin preparation method

The technology of polychlorotrifluoroethylene and chlorotrifluoroethylene is applied in the field of preparation of fluorine-containing polymer materials, which can solve problems such as performance deterioration, pollution, and aggravate PCTFE degradation, and achieve good processability and good heat resistance. Effect

Inactive Publication Date: 2010-02-10
CHANGSHU XINHUA CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] PCTFE is polymerized from chlorotrifluoroethylene (CTFE) as a raw material. In order to obtain PCTFE with sufficient molecular weight to meet the needs of practical applications, a redox initiator system is usually used to polymerize at 0-60 ° C. The oxidant of the initiator system It is persulfate or organic peroxide, and the reducing agent is sodium bisulfite or sodium metabisulfite. The actual polymerization reaction is often more than 30 hours, and the conversion rate of chlorotrifluoroethylene is 60-90%. Although the obtained PCTFE has a strength loss temperature exceeding 260°C (indicating a higher molecular weight), but there are unstable end groups on the molecular chain, which are easily degraded at a processing temperature of 240-280°C, resulting in performance deterioration and severe discoloration
[0006] U.S. Patents US2613202, US2689241 and US5453477 all disclose the preparation of PCTFE, add transition metal ions such as iron ions as accelerators to shorten the polymerization reaction time in the redox initiation system, but the actual polymerization time still reaches 20 hours, and the transition metal ion The introduction further aggravates the degradation of PCTFE at high temperature
[0007] U.S. patents US2751376, US2902477 and US3045000 use solvent-strong oxidant or ozone or chlorine to treat PCTFE powder, which can significantly improve the heat resistance of PCTFE at a processing temperature of 240-280 ° C. However, these treatment processes are difficult to apply industrially. and serious pollution
[0008] The long polymerization time during the preparation of PCTFE, the low conversion rate of chlorotrifluoroethylene, and the poor processability of the obtained PCTFE, such as easy degradation and discoloration at 240-280 ° C, are technical problems that are generally concerned by the industry and have always hoped to be solved. , but also the bottleneck restricting the industrial production of PCTFE

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1-11

[0022] Polymerization was carried out in a 10L vertical stainless steel polymerization reactor with stirring, the amount of deionized water, chlorotrifluoroethylene (CTFE), surfactant and initiator, polymerization temperature, polymerization pressure and polymerization time, CTFE conversion rate , the ZST numerical value of PCTFE and the mass loss of degradability test are shown in Table 1, and in embodiment 1-11, tensio-active agent is perfluorosurfactant, specifically adopts potassium perfluorobutyl sulfonate (KFBS), and initiator adopts The organic initiator with a half-life of 0.1-10 h at 10-50° C. is specifically selected from diisopropyl peroxydicarbonate (IPP).

[0023] After the polymerization reactor has undergone deoxidation treatment, add deionized water and surfactant, the stirring speed of the polymerization reactor is 350n / min, control the temperature in the reactor to the set (designated) temperature, and add the porous silica gel after the adsorption treatment. ...

Embodiment 12-14

[0032] The tensio-active agent potassium perfluorobutane sulfonate (KFBS) in embodiment 1-11 is replaced by ammonium perfluorohexanoate (embodiment 12), perfluoroalkyl oxa nonanoate ammonium (embodiment 13) and perfluoroalkyl oxa nonanoate ammonium (embodiment 13) Sodium fluorononoxybenzene sulfonate (embodiment 14), the ZST numerical value of polymerization reaction time, CTFE conversion ratio, PCTFE and the quality numerical value of degradability test are shown in Table 2, and all the other conditions are with the implementation in the real 1-11 of table 1 Examples 1-3, that is, the remaining conditions of embodiment 12 correspond to embodiment 1, the remaining conditions of embodiment 13 correspond to embodiment 2, and the remaining conditions of embodiment 14 correspond to embodiment 3. The content not mentioned in this embodiment 12-14 is the same as the description of embodiment 1-11.

[0033] Table 2

[0034]

Embodiment 15-17

[0036] The initiator diisopropyl peroxydicarbonate (IPP) in embodiment 1-11 is replaced by diisobutyryl peroxide (embodiment 15) shown in table 3, isobutyl peroxyneodecanoate ( Embodiment 16) and diperfluoropropionyl peroxide (embodiment 17), the ZST numerical value of the time of polymerization reaction, CTFE conversion ratio, PCTFE and the quality numerical value of degradability test are shown in Table 3, and all the other conditions are the same as those shown in Table 1 Embodiment 4-6 in embodiment 1-11, that is: all the other conditions of embodiment 15 are corresponding to embodiment 4, all the other conditions of embodiment 16 are corresponding to embodiment 5 and all the other conditions of embodiment 17 are corresponding to embodiment 6. The contents not described in Examples 15 to 17 are the same as those described in Examples 1-11.

[0037] table 3

[0038] Example

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PUM

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Abstract

The invention provides a polychlorotrifluoroethylene resin preparation method, belonging to the technical field of the preparation of fluoropolymer material. The method comprises the following steps:firstly purifying polytrifluorochloroethylene, then adopting deionized water as medium and using initiator to performing chlorotrifluoroethylene polymerization in the presence of surfactant and obtaining polychlorotrifluoroethylene resin. The invention has the advantage that the polymerization reaction time is shortened to less than 10h, the conversion rate of chlorotrifluoroethylene reach above 90%, the obtained polychlorotrifluoroethylene resin has good heat resistance and processability and degradation and metachromatism can not appear under the processing temperature of 240-280 DEG C. Therefore, the method can meet the demand of industrialized production.

Description

technical field [0001] The invention belongs to the technical field of preparation of fluorine-containing polymer materials, and in particular relates to a preparation method of polychlorotrifluoroethylene resin. Background technique [0002] Polychlorotrifluoroethylene resin (PCTFE) is a thermoplastic with high added value and high performance. As a high-end product, it is often used in harsh environments where other materials cannot be used. When in contact with liquid oxygen, liquid nitrogen and liquefied natural gas, PCTFE has outstanding anti-brittle properties, excellent gas barrier characteristics, and is not affected by ultraviolet and gamma ray radiation. Among refrigerants, PCTFE has outstanding creep resistance characteristics, so it can be used for load bearing parts contacting refrigerant. [0003] PCTFE can be processed by common processes such as injection molding, extrusion, molding and transfer molding. PCTFE is mainly used to make parts of ultra-cold ref...

Claims

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Application Information

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IPC IPC(8): C08F114/24C08F2/44C08F4/34
Inventor 陶惠平杨斌徐俊德
Owner CHANGSHU XINHUA CHEM
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