Epoxy acrylonitrile-butadiene rubber preparation method
A technology of epoxidizing nitrile and epoxidizing reagents, which is applied in the field of polymer materials, can solve the problems of affecting the oil resistance of rubber materials, the degree of epoxidation, and uneven mixing, so as to improve oil resistance and oil resistance Effect
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Embodiment 1
[0025] The polymerization reaction was carried out in a 30L pressure-resistant reactor, and the amount of each monomer added was based on 100 parts of total monomer weight. Before the start of the polymerization reaction, add 310 parts of soft water, 2.0 parts of sodium dodecylbenzene sulfonate, 0.004 parts of Diaobai block, 0.001 parts of EDTA-Fe, 0.001 parts of EDTA-4Na salt, 0.8 parts of t-dodecyl mercaptan and 25 parts. Put the monomer acrylonitrile into the polymerization kettle, vacuum and replace with nitrogen 3 times, then add 75 parts of monomer 1,3-butadiene, 0.04 parts of oxygen scavenger sodium dithionite, and when the polymerization temperature reaches 15℃, add initiator 0.08 parts of dicumyl hydrogen peroxide, polymerization reaction started. During this period, the dry matter content was measured every 3 hours. When the polymerization conversion rate reaches 65%, 0.06 parts of t-dodecanethiol and 6 parts of t-butyl hydroperoxide are added, and the reaction is co...
Embodiment 2
[0029] The polymerization reaction was carried out in a 30L pressure-resistant reactor, and the amount of each monomer added was based on 100 parts of total monomer weight. Before the start of the polymerization reaction, add 370 parts of soft water, 0.006 parts of diaobai block, 0.001 parts of EDTA-Fe, 0.001 parts of EDTA-4Na salt, 3 parts of potassium disproportionated rosinate, 0.7 parts of t-dodecyl mercaptan and 33 parts of monomer monochloride. Acrylonitrile into the polymerization kettle, evacuated and replaced with nitrogen 3 times, then add 67 parts of monomer 1,3-butadiene, 0.09 parts of scavenger sodium dithionite, when the polymerization temperature reaches 15 ℃, add initiator peroxide 0.07 parts of dicumyl hydrogen, polymerization reaction started. When the polymerization conversion rate reaches 65%, 8 parts of peroxyacetic acid and 0.06 parts of t-dodecanethiol are added, and the reaction is continued under vacuum and nitrogen protection. When the polymerization ...
Embodiment 3
[0033] The polymerization reaction was carried out in a 30L pressure-resistant reactor, and the amount of each monomer added was based on 100 parts of total monomer weight. Before the polymerization reaction starts, add 400 parts of soft water, 0.04 parts of diethanolamine, 3 parts of potassium disproportionated rosinate, 0.7 parts of t-dodecanethiol and 30 parts of monomer acrylonitrile to the polymerization kettle, vacuum and replace with nitrogen 3 times, then 70 parts of monomer 2,3-dimethylbutadiene and 0.04 parts of oxygen scavenger N-isopropylhydroxylamine are added, and when the polymerization temperature reaches 30°C, 0.07 parts of initiator potassium persulfate solution is added to start the polymerization reaction. When the polymerization conversion rate reaches 70%, 8 parts of Oxone reagent and 0.05 parts of t-dodecanethiol are added, and the reaction is continued under vacuum and nitrogen protection. When the polymerization conversion rate reaches 85%, add 0.2 part...
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