Polyfluortetraethylene powder and method for producing the same
A technology of polytetrafluoroethylene and its manufacturing method, applied in the field of manufacture of polytetrafluoroethylene fine powder and polytetrafluoroethylene
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Examples
Embodiment 1
[0069] In a 6L horizontal autoclave with a stirrer, 3.55L of pure water (aqueous medium), 54g of ammonium perfluorooctanoate (APFO) in a 10% by mass aqueous solution, 180g of paraffin wax (melting point 62°C), 0.108g of succinic acid ( 30 ppm relative to the aqueous medium), stirring was performed slowly. The inside of the tank was replaced with nitrogen gas while stirring, and then degassed, and the inside of the tank was replaced with TFE gas. The temperature was raised to 80° C., stirred at 200 rpm, the pressure was raised to 2.7 MPa with TFE, and 0.0072 g of ammonium persulfate (APS) (2 ppm relative to the aqueous medium) was added to initiate polymerization. Then, TFE was continuously supplied to keep the pressure inside the tank constant. The stirring speed was set at 135 rpm when 50 g of TFE was consumed, and the stirring speed was set at 120 rpm when 70 g of TFE was consumed. When 3.8 hours had elapsed after the start of the polymerization, the stirring was stopped, ...
Embodiment 2~5 and 7
[0070] Embodiment 2~5 and 7, comparative example 1~4
[0071] Fine powder of PTFE was produced in the same manner as in Example 1 except that the polymerization conditions were changed as shown in Tables 1 and 2. Table 1 shows the standard specific gravity (SSG) of the obtained fine powder and the amount of deposits in the reaction tank.
[0072] In Comparative Example 3, a dispersion was not obtained after the reaction was terminated, and the measurement of the adhesion amount, the solid content concentration as a dispersion, and SSG could not be performed.
Embodiment 6
[0074] Fine powder of PTFE was produced in the same manner as in Example 1 except that the polymerization conditions were changed as shown in Tables 1 and 2. In the polymerization conditions, as for the polymerization pressure, after the initiation of the polymerization, the polymerization was carried out at 0.5 MPa without supplying TFE gas, and the TFE gas was supplied and the pressure was increased to 2.7 MPa after 25 minutes, and then TFE was continuously supplied to thereby The pressure in the tank was kept constant in the same manner as in Example 1.
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Abstract
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