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Batch type bulk technique polypropylene unit flashing kettle nitrogen replacement process

A technology of nitrogen replacement and flash distillation kettle, which is applied in the field of nitrogen replacement technology, can solve the problems of high nitrogen consumption, high pressure and discharge times, hidden dangers of production safety, etc., and achieve the elimination of air pollution and hidden dangers of safe production, short replacement time, The effect of high production efficiency

Inactive Publication Date: 2010-10-20
BEIJING SINO HYPRO PETROCHEM TECH +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The first is the waste of propylene resources. In the process of venting and replacing, a considerable amount of propylene in the exhaust gas of the flash tank is discharged into the atmosphere, resulting in the loss of propylene accounting for about 1-2% of the entire polypropylene process; the second is the waste of nitrogen. , each time the flash tank is pressurized and discharged with nitrogen, the amount of nitrogen consumed is roughly equivalent to the product of the volume of the flash tank and the pressure difference before and after discharge, which has become the main factor for the relatively high nitrogen consumption in the batch bulk polypropylene process; Furthermore, low-concentration propylene gas is directly discharged into the atmosphere, which pollutes the atmosphere and poses hidden dangers to safe production; in addition, due to the relatively large number of pressurization and discharge times, the replacement process is time-consuming.

Method used

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  • Batch type bulk technique polypropylene unit flashing kettle nitrogen replacement process
  • Batch type bulk technique polypropylene unit flashing kettle nitrogen replacement process

Examples

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Effect test

Embodiment 1

[0032] Adopt the continuous nitrogen replacement process of the present invention, after spraying finishes and flash tank decompresses to 120kpa (absolute), begin to flash tank vacuumize, when flash tank is evacuated to 8kpa (absolute) when the evacuation pressure , inject stripping nitrogen, the injection rate of stripping nitrogen is controlled at about 10kpa (absolute) to maintain flash tank pressure, continue the stripping time of 20 minutes, stop vacuuming at last, pressurize flash tank nitrogen to slightly positive pressure, The gas sampling analysis in the flash tank shows that the nitrogen concentration is 99.4%, and the propylene concentration is 0.6%, which meets the discharge requirement of propylene concentration <1%.

Embodiment 2

[0034] Adopt the alternate vacuuming nitrogen replacement process of the present invention, after the material spraying ends and the flash tank is depressurized to 120kpa (absolute), start to vacuumize the flash tank, when the flash tank is evacuated to 8kpa (absolute) When the pressure is high, stop vacuuming, inject pressurized nitrogen to the flash tank 110kpa (absolute), stand still for 30 seconds, and then repeat the above-mentioned vacuuming-nitrogen pressurization-static operation twice. The gas sampling analysis in the flash tank shows that the nitrogen concentration is 99.3%, and the propylene concentration is 0.7%, which meets the discharge requirement of propylene concentration <1%.

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Abstract

The invention relates to a nitrogen replacement process for replacing propylene monomer in batch type bulk technique polypropylene unit by nitrogen, including continuous nitrogen replacement process or alternate evacuation nitrogen replacement process. Propylene gas produced in flashing kettle replacement process can be all drained into a gas holder to be recycled, propylene loss and nitrogen consumption are reduced, thus being beneficial to protection of atmospheric environment and safe production, and replacement efficiency is higher.

Description

technical field [0001] The invention relates to a nitrogen replacement process for replacing propylene monomer in a flash tank with nitrogen in a batch-type bulk polypropylene device. Background technique [0002] The batch bulk polypropylene process is a polypropylene production process independently developed and widely used in China. In the production process of the batch-type bulk polypropylene plant, under the action of catalysts and activators, liquid propylene undergoes polymerization reaction in the polymerization tank under the reaction pressure of 3.6MPa (absolute) and the reaction temperature of 75°C to form solid polypropylene. Acrylic powder. After the polymerization reaction, the remaining propylene in the polymerization tank needs to be recovered to obtain solid polypropylene powder without propylene. Under normal circumstances, the high-pressure recovery of propylene is carried out first, which is to rely on the pressure of the polymerization tank itself to...

Claims

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Application Information

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IPC IPC(8): C08F10/06C08F6/28
Inventor 张国瑞李新张伟冯光陈华蔡海军胥峰
Owner BEIJING SINO HYPRO PETROCHEM TECH
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