Semi-continuous process for preparing organofluorine polymer grafted polyether polyol
A technology of grafting polyether and organic fluorine, which is applied in the field of semi-continuous preparation of organic fluorine polymer and polyether polyol graft copolymer, which can solve the problems of poor adhesion of fluorocarbon paint, wide polymer molecular weight distribution, and equipment production. Low capacity and other problems, to achieve strong adhesion, excellent weather resistance
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Embodiment 1
[0046] (a): Mixing kettle: 268g of vinyl acetate, 16g of undecylenic acid, 117g of unsaturated polyether polyol macromer I, 13g of initiator AIBN, and molecular weight regulator n-C 12 Add SH 4g into a mixing kettle equipped with a temperature controller and an electric stirrer with an effective volume of 1 liter, mix well and control the temperature at 10-15°C.
[0047] (b) Polymerization reactor: Add solvents such as xylene 350g and methyl isobutyl ketone 150g respectively to a pressure-resistant stainless steel polymerization reactor with a temperature controller, nitrogen protection, and an electric stirrer with an effective volume of 2 liters, nitrogen Replace three times, control the oxygen content to less than 60ppm, and raise the temperature to 72±2°C.
[0048] (c) Continuous feeding: The materials in 1 mixing tank are fed into the polymerization at the feed rate (mass) of 52.2g / hour and the feed liquid CTFE of 2 organofluorine monomers is 75g / hour respectively. In th...
Embodiment 2
[0051] Embodiment 2: except that "CTFE is with the feed rate of 75g / hour" in (C) is changed into " TFE is with the feed rate of 65g / hour ", all the other are the same as embodiment 1. The properties of the organic fluoropolymer grafted polyether polyol after drying are shown in Table 1.
Embodiment 3
[0053] (a): Mixing kettle: 185g of vinyl acetate, 16g of undecylenic acid, 200g of unsaturated polyether polyol macromer II, 13g of initiator AIBN, and molecular weight regulator n-C 12 Add SH 4g into a mixing kettle equipped with a temperature controller and an electric stirrer with an effective volume of 1 liter, mix well and control the temperature at 10-15°C.
[0054] (b) Polymerization reactor: Add solvents such as xylene 350g and methyl isobutyl ketone 150g respectively to a pressure-resistant stainless steel polymerization reactor with a temperature controller, nitrogen protection, and an electric stirrer with an effective volume of 2 liters, nitrogen Replace three times, control the oxygen content to less than 60ppm, and raise the temperature to 72±2°C.
[0055] (c) Continuous feeding: The materials in 1 mixing tank are fed into the polymerization at the feed rate (mass) of 52.2g / hour and the feed liquid CTFE of 2 organofluorine monomers is 75g / hour respectively. In t...
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