The invention relates to a new process for SG3 type PVC (
polyvinyl chloride) resin production, which comprises the following steps of: adding a
vinyl chloride monomer, pure water, a dispersant, an initiator and a conventional amount of thermal stabilizer and terminator into a reaction kettle, and meanwhile adding a chain
extender of
maleic acid di-allyl ester into the reaction kettle; wherein the reaction kettle is in a middle size, the
mass proportion of the
monomer, the pure water, the dispersant, the initiator and the chain
extender is 20,000-25,000:30,000-33,000:490-530:120-140:4.5-5.5, and the temperature of
polymerization reaction is 54-58 DEG C. Under the condition of no changing of traditional main production equipment, the invention adjusts the proportioning of relevant auxiliary agents, improves the temperature of the
polymerization reaction, optimizes the control conditions of the production, and shortens the time of the
polymerization reaction for about 60 minutes while adding a proper amount of the chain
extender in a production formula, thereby saving power and
energy consumption, improving production capacity of the equipment, and having safe and stable production
system operation and better economic benefit.