Continuous extrusion method by bulk polymerization of acrylate rubber
A rubber body and acrylate technology, which is applied in the field of reactive continuous extrusion, can solve the problems that the industrialization of acrylate rubber bulk polymerization cannot be realized, the polymerization heat is difficult to control, and the processing and utilization are inconvenient, so as to achieve low ash content, pure polymer, and reaction cycle. short effect
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Embodiment 1
[0027] Component one of embodiment 1 is ethyl acrylate; Component two is acrylic acid; Initiator is azobisisobutyronitrile;
Embodiment 2
[0028] Component one of embodiment 2 is ethyl acrylate; Component two is vinyl chloroacetate; Initiator is azobisisobutyronitrile / cumene hydroperoxide (wherein azobisisobutyronitrile is 0.04, peroxide Hydrogen cumene is 0.04); auxiliary agent is stearic acid
Embodiment 3
[0029] The component one of embodiment 3 is ethyl acrylate / butyl acrylate (wherein ethyl acrylate is 85, and butyl acrylate is 15); Initiator is benzoyl peroxide
[0030] Example 1 is set to
[0031]
Preheat induction section
reaction section
extrusion section
Location
From the feeding port to one-third of the barrel length
1 / 3 to 3 / 4 of the barrel length
Three-quarters of the length of the barrel to the nose
temperature(℃)
50~80
90~120
120~150
[0032] Example 2 is set to
[0033]
Preheat induction section
reaction section
extrusion section
Location
From the feeding port to one-third of the barrel length
1 / 3 to 3 / 4 of the barrel length
Three-quarters of the length of the barrel to the nose
temperature(℃)
65~95
80~150
100~120
[0034] Example 3 is set to
[0035]
Preheat induction section
reaction section
ex...
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