Production method of special polyvinyl chloride resin for battery separator with medium and high degree of polymerization
A technology of polyvinyl chloride resin and battery separator, which is applied in the field of special materials for battery separators, can solve the problems of low yield, low strength, and low quality of separators, and achieves reasonable production technology and formula, and uniform particles. , the effect of particle size distribution concentration
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Embodiment 1
[0032] Add 7.5m to the polymerization kettle 3 desalinated water, 4.5m 3 Vinyl chloride monomer, 10kg of methyl cellulose, 1.8kg of ammonium bicarbonate, 3.5L of neodecanoic acid-2,4,4-trimethylpentyl peroxide were added to the polymerization kettle, stirring at 210rpm, 45°C Polymerization reaction was carried out at 1 hour and 20 minutes, and the stirring speed was transferred to 165rpm to continue the reaction to 10.5 hours, and 0.002kg of acetone thiocarbamate and 0.003m 3 Organosiloxane emulsion. The polyvinyl chloride suspension slurry can be obtained. After the slurry is air-lifted, centrifuged, air-dried, cyclone-dried and bag-dust removed, the finished polyvinyl chloride resin product specially used for battery separators with medium and high polymerization degrees can be obtained. The finished product is tested by adopting the national standard, and the results are shown in Table 1.
Embodiment 2
[0034] Add 7.5m to the polymerization kettle 3 desalinated water, 4.5m 3 Vinyl chloride monomer, 5kg of carboxymethyl cellulose, 5kg of methyl cellulose, 4.5L of ammonium carbonate solution, and 3.0L of diisobutyl peroxide were added to the polymerization kettle, and the polymerization was carried out at a stirring speed of 210rpm and 46°C. Reaction, when reacting for 1 hour and 10 minutes, the stirring speed was adjusted to 155rpm and continued to react for 9.5 hours, adding 0.002kg acetone thiocarbamate and 0.003m 3 Organosiloxane emulsion. The polyvinyl chloride suspension slurry can be obtained. After the slurry is air-lifted, centrifuged, air-dried, cyclone-dried and bag-dust removed, the finished polyvinyl chloride resin product specially used for battery separators with medium and high polymerization degrees can be obtained. The finished product is tested by adopting the national standard, and the results are shown in Table 1.
Embodiment 3
[0036] Add 7.5m to the polymerization kettle 3 desalinated water, 4.5m 3 Vinyl chloride monomer, 5kg of methylcellulose and 5kg of ethylcellulose, 5kg of sodium carbonate, 1.5L of neodecanoic acid-2,4,4-trimethylpentyl peroxide and 2.2L of diisoperoxide Add butyl fat into the polymerization kettle, and carry out the polymerization reaction at 230rpm stirring speed and 48°C. After 1 hour and 15 hours of reaction, adjust the stirring speed to 115rpm and continue the reaction for 8.0 hours, add 0.002kg acetone thiocarbamate and 0.003m 3 Organosiloxane emulsion. The polyvinyl chloride suspension slurry can be obtained. After the slurry is air-lifted, centrifuged, air-dried, cyclone-dried and bag-dust removed, the finished polyvinyl chloride resin product specially used for battery separators with medium and high polymerization degrees can be obtained. The finished product is tested and its results are shown in Table 1.
[0037] Table 1:
[0038] Example
[0039] The ...
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Abstract
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