Continuous production system and production method of polysiloxane
A technology of polysiloxane and production system, applied in the field of continuous production system of polysiloxane, can solve the problems of high viscosity, yellowing of cross-linking, insufficient stirring, etc.
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Embodiment 1
[0142] This embodiment provides a figure 1 The continuous production system of polysiloxane shown includes:
[0143] premixer;
[0144] A polymeric twin-screw extruder connected to the outlet of the premixer;
[0145] A first vacuum pump connected to the exhaust port of the polymeric twin-screw extruder;
[0146] A static mixer connected to the outlet of the polymerization type twin-screw extruder;
[0147] A drop strip type devolatilizer connected to the discharge port of the static mixer;
[0148] The second vacuum pump that links to each other with the vacuum port of described drop bar type devolatilizer;
[0149] The devolatilization type twin-screw extruder that links to each other with the discharge port of described drop bar type devolatilizer;
[0150] The third vacuum pump connected with the vacuum port of the devolatilization type twin-screw extruder;
[0151] A cooling device connected to the outlet of the devolatilization type twin-screw extruder;
[0152] A...
Embodiment 2
[0180] This embodiment provides a figure 1 The continuous production system of polysiloxane shown includes:
[0181] premixer;
[0182] A polymeric twin-screw extruder connected to the outlet of the premixer;
[0183] A first vacuum pump connected to the exhaust port of the polymeric twin-screw extruder;
[0184] A static mixer connected to the outlet of the polymerization type twin-screw extruder;
[0185] A drop strip type devolatilizer connected to the discharge port of the static mixer;
[0186] The second vacuum pump that links to each other with the vacuum port of described drop bar type devolatilizer;
[0187] The devolatilization type twin-screw extruder that links to each other with the discharge port of described drop bar type devolatilizer;
[0188] The third vacuum pump connected with the vacuum port of the devolatilization type twin-screw extruder;
[0189] A cooling device connected to the outlet of the devolatilization type twin-screw extruder;
[0190]A ...
Embodiment 3
[0208] This embodiment provides a figure 1 The continuous production system of polysiloxane shown includes:
[0209] premixer;
[0210] A polymeric twin-screw extruder connected to the outlet of the premixer;
[0211] A first vacuum pump connected to the exhaust port of the polymeric twin-screw extruder;
[0212] A static mixer connected to the outlet of the polymerization type twin-screw extruder;
[0213] A drop strip type devolatilizer connected to the discharge port of the static mixer;
[0214] The second vacuum pump that links to each other with the vacuum port of described drop bar type devolatilizer;
[0215] The devolatilization type twin-screw extruder that links to each other with the discharge port of described drop bar type devolatilizer;
[0216] The third vacuum pump connected with the vacuum port of the devolatilization type twin-screw extruder;
[0217] A cooling device connected to the outlet of the devolatilization type twin-screw extruder;
[0218] A...
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Abstract
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