Method for preparing low-crystal point polyethylene under high pressure by tube process, and low-crystal point polyethylene
A polyethylene and high-pressure technology, applied in the field of polyethylene preparation, can solve the problems of high scrap rate of film blowing, high-end film production, and complicated solutions, and achieve the effect of improving printing quality, reducing film breaking rate and increasing sales price.
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Embodiment 1
[0054] This embodiment is to illustrate the low crystal point polyethylene prepared by the method of the present invention.
[0055] (1) The ethylene monomer is compressed through a compressor; wherein, the filtration accuracy of the pipeline for transporting the ethylene is 1 μm, the content of alkyne in the ethylene monomer is 5 ppm, and the single-cylinder lubricating oil injection amount of the compressor is 2.5 liters / day;
[0056] (2) In the presence of an initiator, the compressed ethylene monomer after step (1) is subjected to an addition polymerization reaction in a reactor; wherein, the initiator is a peroxide, and in the peroxide The content of tert-butyl hydroperoxide is 100ppm; the reaction temperature of the first reaction zone in the reactor is 302°C, and the reaction temperature of the fourth reaction zone is 295°C; the addition polymerization reaction is carried out in the tubular reactor To carry out, the discharge of the tubular reactor is controlled by a p...
Embodiment 2
[0061] This embodiment is to illustrate the low crystal point polyethylene prepared by the method of the present invention.
[0062] (1) Compress ethylene monomer through compressor; Wherein, the filtration precision of the pipeline that transports described ethylene is 1 μm, and the content of alkyne in described ethylene monomer is 5ppm; Compressor single cylinder lubricating oil injection rate is 3 L / day;
[0063] (2) In the presence of an initiator, the compressed ethylene monomer obtained in step (1) is subjected to an addition polymerization reaction in a reactor; wherein, the initiator is a peroxide, and in the peroxide The content of tert-butyl hydroperoxide is 100ppm; increase the reaction temperature of the first reaction zone, be controlled at 305°C, reduce the reaction temperature of the fourth reaction zone, be controlled at 290°C; the addition polymerization reaction is carried out in a tubular reactor The discharge of the tubular reactor is controlled by a puls...
Embodiment 3
[0068] This embodiment is to illustrate the low crystal point polyethylene prepared by the method of the present invention.
[0069] The polyethylene product was prepared in the same manner as in Example 2, except that the reaction pulse level was adjusted to 10, and the reaction pulse period was adjusted to 90 seconds.
[0070] The properties of the prepared polyethylene products are shown in Table 1.
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