Method for producing high-degree of polymerization polyvinyl chloride resin by using suspension method
A technology of polyvinyl chloride resin and high degree of polymerization, which is applied in the field of production of high degree of polymerization polyvinyl chloride resin by suspension method, which can solve the problems of being unable to adapt to high-grade and special processing applications, low compression permanent deformation, and large fluctuations in product quality. Achieve the effects of regular particle shape, low product energy consumption and large batch output
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Embodiment 1
[0017] The DCS control system automatically controls 5kg of ammonium bicarbonate, 32 tons of hot ion-free water, 25 tons of vinyl chloride monomer, 100kg of PVA, 12kg of BNP and 7kg of CNP materials, through the isothermal water feeding technology and the whole closed feeding technology, in the DCS system Under control, automatically join 70m 3 In the polymerization tank, when the polymerization feeding is completed, the reaction temperature reaches 36°C. Under the condition of stirring, the temperature is controlled at 36°C, react for 14 to 16 hours, add 25kg of HER terminator to terminate the polymerization reaction, obtain a slurry of polyvinyl chloride resin with a high degree of polymerization, and remove unreacted vinyl chloride monomer by steam stripping , after centrifugal dehydration and drying, the finished product can be obtained. The HER is the trade name of the terminator, which can be purchased directly from the market, and the manufacturer is Hangzhou Hengxin C...
Embodiment 2
[0019] The DCS control system automatically controls 5kg of sodium carbonate, 32 tons of hot ion-free water, 25 tons of vinyl chloride monomer, 90kg of PVA, 10kg of EHP and 6.5kg of CNP materials, through the isothermal water feeding technology and the whole closed feeding technology, in the DCS system Under control, automatically join 70m 3 In the polymerization tank, when the polymerization feeding is completed, the reaction temperature reaches 38°C. Under the condition of stirring, the temperature is controlled at 38°C, react for 13-15 hours, add 25kg of HER terminator to terminate the polymerization reaction, obtain a slurry of polyvinyl chloride resin with a high degree of polymerization, and remove unreacted vinyl chloride monomer by steam stripping , after centrifugal dehydration and drying, the finished product can be obtained.
Embodiment 3
[0021] The DCS control system automatically controls 5kg of ammonium bicarbonate, 32 tons of hot ion-free water, 25 tons of vinyl chloride monomer, 80kg of PVA, 9kg of BNP and 5kg of CNP materials, through the isothermal water feeding technology and the whole closed feeding technology, in the DCS system Under control, automatically join 70m 3 In the polymerization tank, the reaction temperature reached 40.5°C when the polymerization feeding was completed. Under the condition of stirring, the temperature is controlled at 40.5°C, react for 10 to 12 hours, add 20kg of HER terminator to terminate the polymerization reaction, obtain a slurry of polyvinyl chloride resin with a high degree of polymerization, and remove unreacted vinyl chloride monomer by stripping , after centrifugal dehydration and drying, the finished product can be obtained.
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