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Method for treating butyl acrylate production tail water and extracting sodium acrylate frombutyl acrylate production tail water

A technology of butyl acrylate and sodium acrylate, which is applied in the fields of filtration treatment, water/sewage treatment, water treatment parameter control, etc., can solve the problems of high cost and difficulty in producing tail water of butyl acrylate, and achieves low cost and simple process. Effect

Inactive Publication Date: 2021-10-22
SHANGHAI HONESS ENVIRONMENTAL TECH CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The purpose of the present invention is to provide a method for processing tail water produced by butyl acrylate and extracting sodium acrylate therefrom which can solve the difficulty and high cost of processing tail water produced by butyl acrylate in the prior art

Method used

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  • Method for treating butyl acrylate production tail water and extracting sodium acrylate frombutyl acrylate production tail water
  • Method for treating butyl acrylate production tail water and extracting sodium acrylate frombutyl acrylate production tail water

Examples

Experimental program
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Effect test

Embodiment 1

[0040] Take 500g of butyl acrylate to produce tail water, and the initial indicators of butyl acrylate to produce tail water are: sodium acrylate content 13.20%, COD 137580mg / L, pH value 8.03, chromaticity value 432.

[0041] Add 37.5g of powdered activated carbon to the tail water produced by butyl acrylate, stir at a medium speed for 30 minutes, and filter to obtain the filtrate; evaporate and concentrate the filtrate under vacuum at 67°C, and when the concentration ratio reaches 2.5, collect the evaporative condensate and concentrate; The concentrated solution was transferred to a vacuum drying oven, and dried at 105° C. for 24 hours to obtain solid sodium acrylate, and the evaporated condensate was the treated butyl acrylate tail water.

[0042] The treated butyl acrylate production tail water has a COD concentration of 63mg / L, a chromaticity of 6, and a COD removal rate of 99.95%, which can be collected into pipes or directly discharged. The solid sodium acrylate obtained...

Embodiment 2

[0044] Take 1000g of butyl acrylate to produce tail water, and the initial indicators of butyl acrylate to produce tail water are: sodium acrylate content 13.82%, COD 143450mg / L, pH value 8.11, chromaticity value 444.

[0045] Add 100g of powdered activated carbon to the tail water produced by butyl acrylate, stir at a medium speed for 30 minutes, and filter to obtain the filtrate; evaporate and concentrate the filtrate under vacuum at 70°C, and when the concentration ratio reaches 2.7, collect the evaporative condensate and concentrate; The liquid was transferred to a vacuum drying oven, and dried at 105° C. for 24 hours to obtain a solid sodium acrylate, and the evaporated condensate was the treated butyl acrylate tail water.

[0046] The treated butyl acrylate production tail water has a COD concentration of 54mg / L, a chromaticity of 4, and a COD removal rate of 99.96%, which can be collected into pipes or directly discharged. The solid sodium acrylate obtained by concentra...

Embodiment 3

[0048] Take 1000g of butyl acrylate to produce tail water, and the initial indicators of butyl acrylate to produce tail water are: sodium acrylate content 13.82%, COD 143450mg / L, pH value 8.11, chromaticity value 444.

[0049]Add 100g of resin to the tail water of butyl acrylate production, stir at a medium speed for 30min, filter to obtain a filtrate, add 50g of powdered activated carbon to the filtrate, stir at a medium speed for 30min, and filter to obtain a secondary filtrate; Evaporate and concentrate at 72°C. When the concentration ratio reaches 2.7, collect the evaporated condensate and concentrated liquid; transfer the concentrated liquid to a vacuum drying oven and dry at 105°C for 24 hours to obtain a solid of sodium acrylate, and the evaporated condensed liquid is the processed butyl acrylate production tail water.

[0050] The treated butyl acrylate production tail water has a COD concentration of 76mg / L, a chromaticity of 6, and a COD removal rate of 99.95%, which...

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Abstract

The invention provides a method for treating butyl acrylate production tail water and extracting sodium acrylate from the butyl acrylate production tail water. The method comprises the following steps: adding a powdery activated carbon adsorbent into butyl acrylate production tail water, stirring at a medium speed for 10-30 minutes at a reaction temperature of 20-25 DEG C, filtering, and collecting filtrate; transferring the filtrate to a rotary evaporator, and carrying out evaporation treatment under a vacuum condition to obtain a concentrated solution and an evaporation condensate when the concentration ratio is 2.5-2.7 times, wherein the obtained evaporation condensate is treated butyl acrylate production tail water; and drying the concentrated solution in a vacuum drying oven at 105-120 DEG C until the weight is constant to obtain a sodium acrylate solid. According to the invention, the COD removal rate of the butyl acrylate production tail water treated through the method is 99.95% or above, the COD is lower than 100 mg / L, the tail water can be discharged through a nanotube or directly discharged, the purity of extracted solid sodium acrylate reaches 98.6%, and the problems that the butyl acrylate production tail water is large in treatment difficulty and high in cost are solved.

Description

technical field [0001] The invention relates to the technical field of wastewater treatment, in particular to a method for producing tail water from butyl acrylate and extracting sodium acrylate therefrom. Background technique [0002] In recent years, acrylic acid and its esters, as important industrial derivatives of propylene, have developed rapidly. Acrylic acid is the simplest ethylenic monomer of the unit carboxylate type, which is easy to be copolymerized with other monomers. As a monomer of polymer compounds, the world's total output has exceeded one million tons. One of the factors affecting the development of the acrylic acid and ester industry is the generation of a large amount of waste water, which comes from the production of acrylic acid and acrylate esters, the production of water-soluble resins, dispersants, and flocculants. Due to high concentration and high toxicity, it is difficult to handle and directly biochemically difficult. [0003] At this stage, ...

Claims

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Application Information

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IPC IPC(8): C07C51/42C07C57/07C02F9/10C02F101/34
CPCC07C51/42C02F9/00C02F1/283C02F1/28C02F1/285C02F1/001C02F1/048C02F2209/08C02F2101/34C07C57/04
Inventor 王文标王美静赵志文张凯孙恬乔瑞平
Owner SHANGHAI HONESS ENVIRONMENTAL TECH CORP