Device for producing low-density polyethylene
A low-density polyethylene and ethylene technology, which is applied in the field of high-pressure reactors, can solve problems such as the influence of chemical reaction processes, and achieve the effects of increasing the polymerization rate of branched long chains, improving the degree of branching of long chains and their performance
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Embodiment 1
[0066] exist figure 1 A plant for the production of low density polyethylene is shown producing coating grade low density polyethylene. Such as figure 2 As shown, there is a straight blade turbine blade and a baffle in the tank reactor 3, which are located at 1 / 2 of the height of the tank reactor, forming two reaction zones, and there are 15 double blades in each reaction zone. Pitch paddles, and an anchor paddle at the end of the lowest reaction zone.
[0067] The reaction raw material ethylene is boosted to 30MPa through the first compressor 1, mixed with the recycled ethylene from the oligomer separator 8, and then enters the second compressor 2 to boost the reaction pressure to 300MPa, and the ethylene coming out of the second compressor 2 is divided into Four streams are introduced into the reactor at the upper part 12, the middle part 13 and the lower part 14 of the reactor top 11 and the reactor side respectively, and the free radical initiator di-tert-butyl peroxide...
Embodiment 2
[0070] exist figure 1 A plant for the production of low density polyethylene is shown producing coating grade low density polyethylene. Such as figure 2 As shown, there are two straight blade turbine blades and two baffles in the tank reactor 3, which are located at 1 / 3 and 2 / 3 of the height of the tank reactor, forming three reaction zones, and in each reaction zone There are also 10 two-bladed pitched propellers and an anchored propeller at the end of the lowest reaction zone.
[0071] The reaction raw material ethylene is boosted to 30MPa through the first compressor 1, mixed with the recycled ethylene from the oligomer separator 8, and then enters the second compressor 2 to boost the reaction pressure to 300MPa, and the ethylene coming out of the second compressor 2 is divided into Four streams are introduced into the reactor at the upper part 12, the middle part 13 and the lower part 14 of the reactor top 11 and the reactor side respectively, and the free radical initi...
Embodiment 3
[0074] exist figure 1 A plant for the production of low density polyethylene is shown producing coating grade low density polyethylene. Such as figure 2 As shown, there are three straight-bladed turbine paddles and three baffles in the tank reactor 3, which are located at 1 / 4, 2 / 4 and 3 / 4 of the height of the tank reactor, forming four reaction zones. There are also 8 two-bladed pitched paddles in the reaction zone, and an anchored paddle at the end of the lowest reaction zone.
[0075] The reaction raw material ethylene is boosted to 30MPa through the first compressor 1, mixed with the recycled ethylene from the oligomer separator 8, and then enters the second compressor 2 to boost the reaction pressure to 300MPa, and the ethylene coming out of the second compressor 2 is divided into Four streams are introduced into the reactor at the upper part 12, the middle part 13 and the lower part 14 of the reactor top 11 and the reactor side respectively, and the free radical initia...
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