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Method for inhibiting polymerization of ethylene in compressor equipment in production process of low-density polyethylene

A low-density polyethylene, production process technology, applied in the direction of climate sustainability, sustainable manufacturing/processing, chemical industry, etc., can solve the problems of thinning pipe diameter, entering the pipeline, affecting the reaction, etc., to slow down the self-polymerization of ethylene And fouling phenomenon, improve production efficiency, good effect of polymerization inhibition

Active Publication Date: 2021-06-22
ZHEJIANG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Due to the high pressure of the secondary compressor unit, ethylene self-polymerization may occur. With the extension of the operating time of the device, high-density, high-molecular-weight polymer scaling is easily formed on the inner wall of the intercooler of the secondary compressor, resulting in narrowing of the pipe diameter. , the pressure drop rises, and even the pipeline is blocked; in addition, during the operation of the equipment, the scaling objects will peel off from time to time and enter the pipeline, affecting the reaction
In particular, there is a need for on-line measures to prevent premature self-polymerization and fouling of ethylene in the condenser without stopping the operation, so as to reduce the reduction in production capacity and efficiency caused by regular shutdown and cleaning

Method used

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  • Method for inhibiting polymerization of ethylene in compressor equipment in production process of low-density polyethylene

Examples

Experimental program
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Effect test

Embodiment 1

[0042] use as figure 1 The shown method and device for ethylene polymerization inhibition of the compressor in the production process of low-density polyethylene. The secondary compressor is two-stage compression; the inlet pressure of stage 3 is 24MPa, and the temperature is 38°C; the outlet pressure of stage 5 is 120MPa, and the temperature is 102°C. Inhibitor inlet pressure control is 120MPa. The feed flow rate of the reaction raw material ethylene at the inlet of the secondary compressor 3 is 48.7t / h.

[0043] When it is detected that ln(Px)>10.316-0.0511×Tx, (Px unit bar, Tx unit ℃, the same below), adjust the inhibitor flow valve, add oxygen as a polymerization inhibitor, the addition method is intermittent, and the interval time is 1 minute, the feeding speed is controlled at 0.3kg / h each time it is added. After one month of operation, it was measured that the pressure drop of the intercooler 4 of the secondary compressor units 3, 4, and 5 increased from 2.078MPa to ...

Embodiment 2

[0045] use as figure 1 The shown method and device for ethylene polymerization inhibition of the compressor in the production process of low-density polyethylene. The secondary compressor is two-stage compression; the inlet pressure of stage 3 is 24MPa, and the temperature is 38°C; the outlet pressure of stage 5 is 120MPa, and the temperature is 102°C. Inhibitor inlet pressure control is 120MPa. The feed flow rate of the reaction raw material ethylene at the inlet of the secondary compressor 3 is 48.7t / h.

[0046] When it is detected that ln(Px)>10.316-0.0511×Tx, adjust the polymerization inhibitor flow valve, add oxygen as a polymerization inhibitor, the addition method is continuous, and the oxygen flow rate is 0.3kg / h. After running for one month, the pressure drop of the intercooler 4 of the secondary compressor units 3, 4, and 5 was measured to increase from 2.098MPa to 2.291MPa, and the front and rear pressure drop increased by 0.193MPa. The device needs to be mechanic...

Embodiment 3

[0048] use as figure 1 The shown method and device for ethylene polymerization inhibition of the compressor in the production process of low-density polyethylene. The secondary compressor is two-stage compression; the inlet pressure of stage 3 is 24MPa, and the temperature is 38°C; the outlet pressure of stage 5 is 120MPa, and the temperature is 102°C. Inhibitor inlet pressure control is 120MPa. The feed flow rate of the reaction raw material ethylene at the inlet of the secondary compressor 3 is 48.7t / h.

[0049] When it is detected that ln(Px)>10.316-0.0511×Tx, adjust the polymerization inhibitor flow valve, add air as the polymerization inhibitor, the addition method is intermittent, the interval time is 1 minute, and the feeding speed is controlled at 1.2kg / h. After one month of operation, the pressure drop of the intercooler 4 of the secondary compressor units 3, 4, and 5 was measured to increase from 2.102MPa to 2.507MPa, and the front and rear pressure drop increase...

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Abstract

The invention discloses a method for inhibiting polymerization of ethylene in compressor equipment in the production process of low-density polyethylene. According to the method, in a tubular reactor low-density polyethylene production process, a polymerization inhibitor is added into a secondary compressor to prevent ethylene from self-polymerization, pressure drop rise of a cooler and scaling of equipment are effectively avoided, and the polymerization inhibitor can be used as an initiator in a reactor behind the compressor; and the polymerization inhibitor is oxygen or air. The problems that in the production process of high-pressure polyethylene, ethylene raw materials are self-polymerized too early, and a cooler in a secondary compressor is prone to scaling are effectively solved. The method has the advantages that the polymerization inhibition effect is good, operation is easy and convenient, production is not affected, scaling of the compressor cooler can be eliminated on line, and meanwhile the polymerization inhibitor can be efficiently utilized as an initiator of the follow-up procedure without aftertreatment.

Description

technical field [0001] The invention belongs to the field of chemical industry, and in particular relates to a method for inhibiting polymerization of ethylene in the production process of a low-density polyethylene tubular method. Background technique [0002] As is known in the art, high pressure polyethylene polymerization processes are carried out in autoclaves or tubular reactors, usually using oxygen or organic free radical initiators, especially peroxides, as initiators to obtain low density ethylene polymers (LDPE). Compared with the kettle-type process, the high-pressure tubular-type polyethylene process has the advantages of high conversion rate per pass, low monomer consumption, long production cycle, large production capacity, simple and reliable equipment, etc., so the tubular-type process is widely used in my country more extensive. [0003] The high-pressure tubular process includes compression unit, polymerization unit, separation and gas circulation unit, ex...

Claims

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Application Information

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IPC IPC(8): C08F2/00C08F210/16C08F210/06C08F2/38
CPCC08F2/007C08F2/005C08F210/16C08F210/06C08F2/38Y02P20/10
Inventor 任聪静范小强王靖岱历伟黄正梁孙婧元杨遥陈毓明阳永荣
Owner ZHEJIANG UNIV
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