A method for initiating a polymerization reaction
A technology of polymerization reaction and polymerization reactor, which is applied in the field of initiation of solution method ethylene propylene rubber polymerization reaction, can solve the problems of reaction efficiency reduction, catalyst poisoning, etc., achieve stable production and operation, and solve the effect of catalyst activity reduction
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Embodiment 1
[0019] The polymerization reactor is traced externally with a heat tracing pipe with a pipe diameter of 1 / 2 inch, and the heat tracing pipe is arranged on the side wall and the bottom of the polymerization reactor in a winding manner. The volume of the polymerization reactor is 30 cubic meters, and the number of heat tracing pipes is 8. 2barg saturated steam is introduced into the heat tracing pipe, the distance between adjacent heat tracing pipes is 50mm, the flow rate of steam in the heat tracing pipe is 5m / s, the temperature of the material in the polymerization reactor rises by 30°C, and the polymerization reaction caused by each start-up Time control is 5 hours.
Embodiment 2
[0021] The polymerization reactor is traced externally with a heat tracing pipe with a pipe diameter of 11 / 2 inches, and the heat tracing pipe is arranged on the side wall and the bottom of the polymerization reactor in a winding manner. The volume of the polymerization reactor is 100 cubic meters, and the number of heat tracing pipes is 2. 9barg saturated steam is introduced into the heat tracing pipe, the distance between adjacent heat tracing pipes is 300mm, the flow rate of steam in the heat tracing pipe is 30m / s, the temperature of the material in the polymerization reactor rises by 80°C, and the polymerization reaction caused by each start-up Time control is 0.5 hours.
Embodiment 3
[0023] The polymerization reactor is traced externally with a heat tracing pipe with a pipe diameter of 3 / 4 inch, and the heat tracing pipe is arranged on the side wall and the bottom of the polymerization reactor in a winding manner. The volume of the polymerization reactor is 80 cubic meters, and the number of heat tracing pipes is 5. 7barg saturated steam is fed into the heat tracing pipe, the distance between adjacent heat tracing pipes is 100mm, the flow rate of steam in the heat tracing pipe is 25m / s, the temperature of the material in the polymerization reactor rises by 50°C, and the polymerization reaction caused by each start-up Time control is 3.5 hours.
[0024] The polymerization initiation method used in Examples 1 to 3 of the present invention avoids the introduction of water into the polymerization reaction system, makes the production and operation of the traditional solution method ethylene-propylene rubber device stable, and solves the catalyst activity cause...
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