Preparation process of chlorinated polyvinyl chloride resin
A technology of chlorinated polyvinyl chloride and polyvinyl chloride resin, which is applied in the field of production of chlorinated polyvinyl chloride resin, can solve the problems of not strictly controlling the speed of chlorine flow, poor heat resistance stability, and drop in reaction pressure, so as to ensure chlorination Uniformity, ensuring heat resistance stability, and increasing the effect of heat resistance stability
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Embodiment 1
[0025] In a 100L enamel reaction kettle, add 15Kg of PVC resin with a polymerization degree of 700 and 85Kg of deionized water, and use different types of initiators under the same operating conditions except for different initiator conditions. The amount of the initiator is 0.5% (wt %) of PVC consumption, namely 250g weight concentration is that 30% hydrogen peroxide, 75g azobisisobutyronitrile and 100g weight concentration are 75% dibenzoyl peroxide, then add 300g weight concentration 25% After the silica sol, feed nitrogen for 30 minutes, and at the same time, feed steam into the jacket to raise the temperature to 60°C, turn off nitrogen, feed chlorine gas with a flow rate of 12L / min for 5 minutes, and then close the tail gas valve. Minutes; heat up to 115°C and keep the temperature constant, adjust the chlorine flow rate of 24L / min for 90 minutes; heat up to 130°C and keep the temperature constant, adjust the chlorine flow rate of 12L / min for 45 minutes, at this time the to...
Embodiment 2
[0029] In a 100L enamel reaction kettle, add 15Kg of PVC resin with a polymerization degree of 700 and 85Kg of 10% concentration hydrochloric acid, and use different types of initiators under the same operating conditions except for different initiator conditions. The amount of the initiator is 0.5% (wt %) of PVC consumption, namely 250g weight concentration is that 30% hydrogen peroxide, 75g azobisisobutyronitrile and 100g weight concentration are 75% dibenzoyl peroxide, then add 300g weight concentration 25% After the silica sol, feed nitrogen for 30 minutes, and at the same time, feed steam into the jacket to raise the temperature to 60°C, turn off nitrogen, feed chlorine gas with a flow rate of 12L / min for 5 minutes, and then close the tail gas valve. Minutes; heat up to 115°C and keep the temperature constant, adjust the chlorine flow rate of 24L / min for 90 minutes; heat up to 130°C and keep the temperature constant, adjust the chlorine flow rate of 12L / min for 45 minutes,...
Embodiment 3
[0033] In a 100L enamel reaction kettle, add 15Kg of PVC resin with a polymerization degree of 700 and 85Kg of deionized water, and use different types of initiators under the same operating conditions except for different initiator conditions. The amount of the initiator is 1.0% (wt %) of PVC consumption, promptly add the dibenzoyl peroxide of 500g weight concentration 30% hydrogen peroxide, 150g azobisisobutyronitrile and 200g weight concentration 75%, then add 300g weight concentration 25% silicon After the sol, feed nitrogen for 30 minutes, and at the same time, feed steam into the jacket to raise the temperature to 60°C, turn off the nitrogen, feed chlorine gas with a flow rate of 12L / min for 5 minutes, then close the tail gas valve, keep the temperature at 100°C, and maintain the chlorine flow rate for 40 minutes Raise the temperature to 115°C and keep the temperature constant, adjust the chlorine flow rate of 24L1 / min for 90 minutes; raise the temperature to 130°C and ke...
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