Preparation method of high polymerization degree delustering polyvinyl chloride resin
A technology of polyvinyl chloride resin and high degree of polymerization, which is applied in the preparation of polyvinyl chloride resin and the field of preparation of high degree of polymerization matting polyvinyl chloride resin, which can solve the problems of insufficient matting effect, increased cost, and decreased mechanical properties. Achieve good matting effect and solve the effect of rising costs
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Embodiment 1
[0031] 4g of ammonium bicarbonate, 10kg of non-ionized water, 6kg of vinyl chloride monomer, 18g of PVA, 9g of HPMC, 22g of CNP initiator, 58g of polyethylene glycol dimethacrylate and other materials were added to a 20 liter polymerizer. After cold stirring for 5 to 10 minutes, the temperature was raised to a reaction temperature of 38°C. After the polymerization reaction pressure is reduced by 0.15MPa, the polymerization reaction is terminated, the monomer is recovered under self-pressure, and the material is discharged. After steam stripping, degassing, centrifugal dehydration, and drying, the finished product of high polymerization degree matting resin can be obtained.
[0032] The PVA in this example is 82% polyvinyl alcohol with high alcoholysis degree, and the HPMC is hydroxypropyl methylcellulose with a viscosity of 40 mPa·s, a methoxy content of 29%, and a hydroxypropyl content of 6%. .
Embodiment 2
[0034] 3.6g of sodium bicarbonate, 10kg of non-ionized water, 6kg of vinyl chloride monomer, 18g of PVA1, 15g of PVA2, 22g of CNP initiator, 45g of triallyl cyanurate and other materials were added to a 20 liter polymerization vessel. After cold stirring for 5 to 10 minutes, the temperature was raised to a reaction temperature of 38°C. When the conversion rate is 40%, 20 g of polyethylene glycol dimethacrylate is added. After the polymerization reaction pressure is reduced by 0.15 MPa, the polymerization reaction is terminated, the monomer is recovered under self-pressure, and the material is discharged. After steam stripping, degassing, centrifugal dehydration, and drying, the finished product of high polymerization degree matting resin can be obtained.
[0035] In this example, PVA1 is polyvinyl alcohol with a high degree of alcoholysis of 80%, and PVA2 is polyvinyl alcohol with a degree of medium alcoholysis of 70%.
Embodiment 3
[0037] 4g of ammonium bicarbonate, 10kg of non-ionized water, 6kg of vinyl chloride monomer, 16g of PVA, 8g of HPMC, 19g of CNP initiator, 58g of polyethylene glycol dimethacrylate and other materials were added to a 20 liter polymerizer. After cold stirring for 5-10 minutes, the temperature was raised to a reaction temperature of 40°C. After the polymerization reaction pressure is reduced by 0.1MPa, the polymerization reaction is terminated, the monomer is recovered under self-pressure, and the material is discharged. After steam stripping, degassing, centrifugal dehydration, and drying, the finished product of high polymerization degree matting resin can be obtained.
[0038] The PVA in this example is 82% polyvinyl alcohol with high alcoholysis degree, and the HPMC is hydroxypropyl methylcellulose with a viscosity of 40 mPa·s, a methoxy content of 29%, and a hydroxypropyl content of 6%. .
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