A kind of auxiliary agent for PVC processing and preparation method thereof
A technology of additives and initiators, applied in the field of PVC processing additives and its preparation, can solve the problems of poor performance of PVC products, poor surface finish of products, increase of product volume cost, etc., to promote uniform plasticization of PVC , good fluidity, and the effect of improving processing performance
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Embodiment 1
[0028] The PVC processing aid of the present invention has a core-shell structure with calcium maleate-styrene copolymer as the core and methyl methacrylate as the shell, and the intrinsic viscosity is 3.0.
[0029] In parts by weight, the PVC processing aid includes 100 parts of calcium maleate monomer, 10 parts of styrene monomer and 15 parts of methyl methacrylate monomer, and is formed by polymerizing the amount of monomer get.
[0030] The preparation method of auxiliary agent for PVC processing of the present invention comprises the following steps:
[0031] (1) in the reactor that stirring, condenser are housed, add quantitative distilled water, calcium maleate monomer, initiator A, emulsifier, dispersant, styrene monomer, stir 10 minutes to obtain pre-emulsion;
[0032] (2) pass into N 2 , and the temperature of the pre-emulsion was raised to 40°C, and the heat preservation reaction was carried out under constant stirring for 0.5 hours to obtain the core layer emulsi...
Embodiment 2
[0042] The difference between embodiment 2 and embodiment 1 is:
[0043]The PVC processing aid has a core-shell structure with calcium maleate-α-methylstyrene copolymer as the core and ethyl methacrylate as the shell, and has an intrinsic viscosity of 10.0.
[0044] In parts by weight, the PVC processing aids include 100 parts of calcium maleate monomer, 25 parts of α-methylstyrene monomer and 40 parts of ethyl methacrylate monomer, and by polymerizing the obtained from the monomer.
[0045] The preparation method of described PVC processing auxiliary agent, comprises the steps:
[0046] (1) In the reaction kettle equipped with stirring and condenser, add quantitative distilled water, calcium maleate monomer, initiator A, emulsifier, dispersant, α-methylstyrene monomer, and stir for 10 minutes to obtain pre-emulsion;
[0047] (2) pass into N 2 , and the temperature of the pre-emulsion was raised to 90°C, and the reaction was kept under constant stirring for 5 hours to obta...
Embodiment 3
[0055] The difference between embodiment 3 and embodiment 1 is:
[0056] The PVC processing aid has a core-shell structure with calcium maleate-tert-butylstyrene copolymer as the core and n-butyl methacrylate as the shell, and has an intrinsic viscosity of 7.0.
[0057] In parts by weight, the PVC processing aids include 100 parts of calcium maleate monomer, 18 parts of tert-butyl styrene monomer and 32 parts of n-butyl methacrylate monomer, and by polymerizing the obtained from the monomer.
[0058] The preparation method of described PVC processing auxiliary agent, comprises the steps:
[0059] (1) In the reaction kettle equipped with stirring and condenser, add quantitative distilled water, calcium maleate monomer, initiator A, emulsifier, dispersant, tert-butylstyrene monomer, and stir for 10 minutes to obtain the preliminary Emulsion;
[0060] (2) pass into N 2 , and the temperature of the pre-emulsion was raised to 60°C, and the reaction was kept under constant stirr...
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