System and process for enhancing ethylene polymerization
An ethylene polymerization and ethylene technology, applied in the field of polymer preparation, can solve the problems of insufficient mixing between materials and low polymerization efficiency, and achieve the effects of improving mixing efficiency, increasing phase boundary area, and improving polymerization efficiency.
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Embodiment 1
[0092] The above-mentioned system and the above-mentioned process are used to prepare polyethylene, wherein the catalyst in the step 2 is titanium tetrachloride.
[0093] The viscosity reducing agent in the described step 2 selects n-hexane for use.
[0094] The comonomer in step 3 is selected from short-chain α-olefins.
[0095] In the step 3, oxygen is selected as the initiator, and the initiator content is 0.003% of the ethylene content.
[0096] In the step 5, the polymerization temperature is 230° C., and the reaction pressure is 140 MPa.
[0097] The obtained polyethylene was tested, and it was found that the PDI of the product polyethylene was 1.93, and the conversion rate of ethylene was 93.5%.
Embodiment 2
[0099] The above-mentioned system and the above-mentioned process are used to prepare polyethylene, wherein the catalyst in the step 2 is diethylaluminum chloride.
[0100] The viscosity reducing agent in the described step 2 selects n-hexane for use.
[0101] The comonomer in step 3 is vinyl acetate.
[0102] In the step 3, oxygen is selected as the initiator, and the initiator content is 0.004% of the ethylene content.
[0103] In the step 5, the polymerization temperature is 245° C., and the reaction pressure is 160 MPa.
[0104] The obtained polyethylene was tested, and it was found that the PDI of the product polyethylene was 1.81, and the conversion rate of ethylene was 94.8%.
Embodiment 3
[0106] The above-mentioned system and the above-mentioned process are used to prepare polyethylene, wherein the catalyst in the step 2 is a mixed solvent of titanium tetrachloride and diethylaluminum chloride.
[0107] The viscosity reducing agent in the described step 2 selects n-hexane for use.
[0108] The comonomer in step 3 is selected from acrylate.
[0109] Oxygen is selected as the initiator in the step 3, and the initiator content is 0.006% of the ethylene content.
[0110] In the step 5, the polymerization temperature is 255° C., and the reaction pressure is 180 MPa.
[0111] The obtained polyethylene was detected, and it was found that the PDI of the product polyethylene was 1.55, and the conversion rate of ethylene was 96.7%.
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