Production method of ethylene-vinyl acetate copolymer resin for solar cell sealing sheet and resin produced by the production method
A vinyl acetate and manufacturing method technology, applied in photovoltaic power generation, etc., can solve the problems of low economy, weak adhesion, peeling, etc., and achieve the effects of low moisture permeability, excellent long-term durability, and high resistance
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Embodiment 1
[0047] 76% by weight of ethylene monomer and 24% by weight of vinyl acetate monomer were injected into the tubular reactor as free radical generation initiators to make tert-butyl peroxide 2-ethylhexanoate (TBPO), pivalic acid peroxide The weight ratio of the mixture of tert-butyl ester (TBPV), tert-butyl peroxyneodecanoate (TBND), and tert-butyl peroxy-3,5,5-trimethylhexanoate (TBPIN) is 1:0.2:0.4 : 0.1, 1800ppm compared with ethylene and vinyl acetate monomers, sent to the tubular reactor (tubularreactor) using a high pressure pump, at a polymerization pressure of 2650kg / cm 2 , The EVA resin was produced under the polymerization conditions of a polymerization temperature of 240° C. and a polymerization time of 5 minutes.
Embodiment 2
[0049] 76% by weight of ethylene monomer and 24% by weight of vinyl acetate monomer are injected into the tubular reactor, as a catalyst for generating free radicals, tert-butyl peroxide 2-ethylhexanoate (TBPO), pivalic acid peroxide The weight ratio of the mixture of tert-butyl ester (TBPV), tert-butyl peroxyneodecanoate (TBND), and tert-butyl peroxy-3,5,5-trimethylhexanoate (TBPIN) is 1:0.4:0.6 : 0.1, 1500ppm compared with ethylene and vinyl acetate monomer, using high pressure pump to send to tubular reactor (tubular reactor), at a polymerization pressure of 2650kg / cm 2 , The EVA resin was produced under the polymerization conditions of a polymerization temperature of 200° C. and a polymerization time of 5 minutes.
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