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.