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Clean production method of chlorinated polyethylene

A technology for chlorinated polyethylene and cleaner production, applied in the field of cleaner production of chlorinated polyethylene, can solve the problems of difficulty in recycling, large discharge of waste water, heavy environmental pollution, etc. Process efficient effect

Active Publication Date: 2014-04-30
WEIFANG YAXING GRP CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantage of the aqueous phase suspension method is that water is used as the chlorination medium. After the chlorination reaction, the by-product hydrogen chloride is absorbed to form dilute hydrochloric acid with a weight concentration of 5%-6%. Due to the low concentration of hydrochloric acid, it is difficult to recycle and the waste water discharge is large. Heavy environmental pollution; the production process of the hydrochloric acid phase suspension method uses hydrochloric acid with a weight concentration of about 20% to prepare a hydrochloric acid phase suspension. After the concentrated acid is removed, the slurry needs to be further washed, and some dilute acid with a lower concentration will still be produced during the further washing process.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] at 12.5m 3 In the chlorination reactor, inject 9720Kg of hydrochloric acid solution with a concentration of 17wt%, add 1100Kg of high-density polyethylene, 0.6Kg of fatty alcohol polyoxyethylene ether and 12Kg of talcum powder, stir for 5 minutes, prepare a suspension solution, and seal the reactor.

[0020] Pass 900Kg liquid chlorine into the suspension solution in the reactor to carry out chlorination reaction, the reaction temperature is 50-130° C., and the reaction time is 3.5 hours to obtain chlorinated polyethylene slurry.

[0021] After cooling down, the chlorinated polyethylene slurry is transported to the filter washer, and through the synchronous cooperation of the rotating filter disc and the filter controller, the filter is divided into two sections to realize two-stage cleaning of the slurry. Stage filtration deacidification, the chlorinated polyethylene slurry passes through the first stage filter section, the concentrated hydrochloric acid contained in th...

Embodiment 2

[0024] at 60m 3 In the chlorination reactor, inject 43200 Kg of hydrochloric acid solution with a concentration of 22wt%, add 5500 Kg of high-density polyethylene, 1.5 Kg of polyvinylpyrrolidone and 55 Kg of amorphous silicon dioxide, stir for 10 minutes, prepare a suspension solution, and seal the reactor .

[0025] Pass 4800Kg liquid chlorine into the suspension solution in the reactor to carry out chlorination reaction, the reaction temperature is 30-130° C., and the reaction time is 5 hours to obtain chlorinated polyethylene slurry.

[0026] After cooling down, the chlorinated polyethylene slurry is transported to the filter washer, and through the synchronous cooperation of the rotating filter disc and the filter controller, the filter is divided into two sections to realize two-stage cleaning of the slurry. Stage filtration deacidification, the chlorinated polyethylene slurry passes through the first stage filter section, the concentrated hydrochloric acid contained in ...

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Abstract

The invention discloses a clean production method of chlorinated polyethylene. The clean production method adopts a hydrochloric acid phase suspension process which comprises the following steps: preparation of a supernatant solution, a chlorination process, a deacidification process, a centrifugation and drying process. The deacidification process includes two stages of filtration and deacidification; a chlorinated polyethylene slurry material is subjected to a first stage of filtration, a concentrated hydrochloric acid contained in the slurry material is filtered out and put into a concentration acid storage tank, subsequently the slurry material is subjected to a second stage of filtration, the acid residue in the slurry material is washed by water and filtered out to form a diluted hydrochloric acid, and then the diluted hydrochloric acid is put into a diluted acid storage tank. The production method disclosed by the invention has the beneficial effects that by the two stages of filtration and deacidification, the concentrated hydrochloric acid in the slurry material is totally recycled and sold after the chlorination reaction, and the diluted hydrochloric acid generated by washing the slurry material after the reaction is totally recycled as well, thus zero emission of acidic water generated after the chlorination reaction and during filtration and washing is realized, the energy conservation and emission reduction effects are obvious, the production cost is further lowered, and the production process is efficient, clean and environment-friendly.

Description

technical field [0001] The invention relates to a clean production method of chlorinated polyethylene. Background technique [0002] Chlorinated polyethylene is a polymer material obtained by chlorination substitution reaction of high-density polyethylene. It is mainly used as a resin impact modifier and synthetic rubber. [0003] At present, the main method of producing chlorinated polyethylene at home and abroad is the suspension method. There are two production processes of aqueous phase suspension method and hydrochloric acid phase suspension method in the production of chlorinated polyethylene by suspension method. The disadvantage of the aqueous phase suspension method is that water is used as the chlorination medium. After the chlorination reaction, the by-product hydrogen chloride is absorbed to form dilute hydrochloric acid with a weight concentration of 5%-6%. Due to the low concentration of hydrochloric acid, it is difficult to recycle and the waste water discharg...

Claims

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Application Information

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IPC IPC(8): C08F10/02C08F8/22
Inventor 杨雷李白贤韩风钟棉军赵文斌隋树鹏孙岩
Owner WEIFANG YAXING GRP CO LTD
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