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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

Active Publication Date: 2011-06-08
上海高分子功能材料研究所
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] At present, the synthesis of acrylate rubber in industry mainly includes suspension polymerization, solution polymerization, and emulsion polymerization. Among them, emulsion polymerization is more common, but the three methods of emulsion, suspension, and solution all face a series of problems, such as the need for a large amount of solvent or water. Recycling, the synthesis process is complicated, and the additives remaining in the polymer also bring inconvenience to the later processing and utilization
The traditional bulk polymerization method is difficult to control the heat of polymerization, so the industrialization of acrylate rubber bulk polymerization cannot be realized

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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PUM

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Abstract

A continuous extrusion method by the bulk polymerization of acrylate rubber is characterized in that: a reaction component I, a reaction component II, an initiator and an addition agent are mixed according to a proportioning ratio to form a mixed solution according to a certain mixture ratio; then the mixed solution is injected into an extruder protected under N2 for reaction and extrusion; and finally solid materials of various shapes are obtained. According to parts by weight, the mixed solution comprises: 100 parts of the component I, 0-30 parts of the component II, 0.01-5 parts of the initiator and 0-5 parts of the addition agent. The method has the following advantages of: pure polymer in the bulk polymerization and lower ash content, simple synthesis formula and less intermittent equipment, and less working procedures due to reaction under the solvent-free condition, shortened process, reduced cost and improved production efficiency.

Description

technical field [0001] The invention relates to a reaction continuous extrusion method of bulk polymerization of acrylate rubber, in particular to the realization of the reaction continuous extrusion of bulk polymerization of acrylate rubber synthesis on an extruder. Background technique [0002] The application of the principle of reactive extrusion to the synthesis of high polymers first appeared in the 1960s. At present, polyurethane and polylactic acid have been applied. [0003] At present, the synthesis of acrylate rubber in industry mainly includes suspension polymerization, solution polymerization, and emulsion polymerization. Among them, emulsion polymerization is more common, but the three methods of emulsion, suspension, and solution all face a series of problems, such as the need for a large amount of solvent or water. Recycling, complex synthesis process, and additives remaining in the polymer also bring inconvenience to later processing and utilization. The tr...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F2/02C08F20/10
Inventor 穆肖斌孙国辉毛阿康吴浩文
Owner 上海高分子功能材料研究所
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