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
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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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