Synthesis method of polyethylene
A synthesis method and polyethylene technology, applied in the field of olefin polymerization, can solve the problems of inability to produce bimodal polyethylene, high requirements for catalyst supports, and low content of reinforcing components, and achieve reduced solvent separation and recovery equipment, convenient operation, and reduced Effect of fines content
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Embodiment 1
[0065] exist figure 1 In the shown polymerization reaction system, linear low density polyethylene (LLDPE) is produced, the polymerization reaction temperature of the loop reactor is 60°C, and the reaction pressure is 40 bar. Under the action of the Z-N catalyst system, ethylene undergoes polymerization reaction in the reactor. The solvent is isopentane. The slurry discharged from the loop reactor is concentrated by 8% in the hydrocyclone and enters the fluidized bed reactor under the action of pressure difference. The polymerization temperature of the fluidized bed reactor is 88°C and the pressure is 23bar. Under the action of the Z-N catalyst system, ethylene and 1-butene continue to undergo copolymerization reaction, and the reaction materials include hydrogen, ethylene, and 1-butene. The unreacted gas circulating material is discharged from the top of the fluidized bed reactor, and the temperature of the outlet material after being pressurized by the compressor and cooler...
Embodiment 2
[0068] exist figure 2 In the shown polymerization reaction system, linear low density polyethylene (LLDPE) is produced, the polymerization reaction temperature of the loop reactor is 60°C, and the reaction pressure is 40 bar. Under the action of the Z-N catalyst system, ethylene undergoes polymerization reaction in the reactor. The solvent is isopentane. The slurry discharged from the loop reactor is concentrated by 8% in the hydrocyclone and enters the fluidized bed reactor under the action of pressure difference. The polymerization reaction temperature of the fluidized bed reactor is 87°C and the pressure is 25 bar. Under the action of the Z-N catalyst system, the copolymerization reaction of ethylene and 1-butene continues, and the reaction materials include hydrogen, ethylene and 1-butene. The unreacted gas circulating material is discharged from the top of the fluidized bed reactor, and the temperature of the outlet material after being pressurized by the compressor and...
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