Fluorocopolymer and its applications
A technology of copolymer and tetrafluoroethylene, applied in coating, layered products, transportation and packaging, etc., can solve problems such as insufficient copolymerization ability, and achieve good interlayer adhesion performance, good heat resistance, and good fuel shielding performance effect
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Embodiment 1
[0067] Air was removed from a polymerization autoclave equipped with a stirrer and an inner capacity of 1.2 liters, and then 1131 g of 1,3-dichloro-1,1,2,2,3-pentafluoropropane (manufactured by Asahi Glass Co., Ltd., hereinafter called AK225cb) and 120.1 grams of CF 2 =CFO(CF 2 ) 3 F. The inside of the polymerization autoclave was then heated to 50°C, 73 grams of TFE was added, and the pressure was increased to 0.43 MPa / G. 1 cm3 of an AK225cb solution containing 0.1% by mass of (perfluorobutyryl) peroxide was added as a polymerization initiator solution to initiate polymerization, and thereafter 1 cm3 of this polymerization initiator solution was added every 10 minutes. In addition, TFE was continuously fed to maintain the pressure at 0.43 MPa / G during the polymerization. In addition, an AK225cb solution containing 0.3% by mass of NAH was continuously added in an amount equal to 0.1 mol% of the mole amount of TFE added during the polymerization. Five hours after initiatio...
Embodiment 2
[0072] The air in the polymerization autoclave used in Example 1 was removed, then 500AK225cb, 600 g of HFP and 50 g of TFE were charged, and the inside of the polymerization autoclave was heated to 50°C. The pressure becomes 0.98 MPa / G. 1 cm3 of an AK225cb solution containing 0.25% by mass of bis(perfluorobutyryl) peroxide was added as a polymerization initiator solution to initiate polymerization, and 1 cm3 of this polymerization initiator solution was added every 10 minutes thereafter. In addition, TFE was continuously fed to maintain the pressure at 0.98 MPa / G during the polymerization. In addition, an AK225cb solution containing 0.3% by mass of NAH was continuously added in an amount equal to 0.1 mol% of the continuously added molar amount of TFE. Four hours and 20 minutes after initiation of the polymerization, at which time 50 g of TFE had been added, the temperature in the polymerization autoclave was lowered to room temperature while unreacted monomers were vented. ...
Embodiment 3
[0077] Remove the air in the polymerization autoclave used in Example 1, then add 500AK225cb, 600 grams of HFP, 25 grams of CF 2 =CFO(CF 2 ) 3 F and 50 g of TFE, and the inside of the polymerization autoclave was heated to 50°C. The pressure becomes 0.96 MPa / G. 1 cm3 of an AK225cb solution containing 0.25% by mass of bis(perfluorobutyryl) peroxide was added as a polymerization initiator solution to initiate polymerization, and 1 cm3 of this polymerization initiator solution was added every 10 minutes thereafter. TFE was continuously fed to maintain the pressure at 0.96 MPa / G during the polymerization. In addition, an AK225cb solution containing 0.3% by mass of NAH was continuously added in an amount equal to 0.1 mol% of the continuously added molar amount of TFE. Four hours and 40 minutes after initiation of the polymerization, at which point 50 g of TFE had been added, the temperature in the polymerization autoclave was lowered to room temperature while unreacted monomers...
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