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Method for separating and refining industrial benzoic acid from PTA (pure terephthalic acid) process wastewater

A technology for benzoic acid and wastewater, applied in the chemical industry, separation/purification of carboxylic acid compounds, sustainable manufacturing/processing, etc., can solve problems such as difficult separation of terephthalic acid and benzoic acid, achieve temperature reduction, save energy Energy and water consumption reduction effects

Inactive Publication Date: 2013-01-09
江苏华旭环保股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Other units such as Liaoyang Petrochemical, Yizheng Chemical Fiber, and Luoyang Petrochemical have published articles. Although their processes are different, it is difficult to separate terephthalic acid from benzoic acid.

Method used

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Embodiment Construction

[0017] A method for separating and refining industrial benzoic acid from PTA process wastewater, comprising the following steps:

[0018] (1) Heat the PTA process wastewater to 95-105°C, and centrifuge through a horizontal scraper discharge centrifuge to obtain terephthalic acid solids and mixed liquids containing benzoic acid, cobalt, and manganese;

[0019] (2) Cool the mixed liquid containing benzoic acid, cobalt, and manganese through a jacketed reactor, so that the temperature of the mixed liquid drops to 20-30°C, and the cooled mixed liquid is filtered by a diaphragm plate and frame filter press to obtain Benzoic acid first product; The fluid in the jacket of described jacketed reactor is water; The waste heat of described jacketed reactor is collected by plate heat exchanger;

[0020] (3) The primary product of benzoic acid is dried by a belt dryer, and the heat energy of the belt dryer is the waste heat collected by the plate heat exchanger;

[0021] (4) The primary ...

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PUM

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Abstract

The invention discloses a method for separating and refining industrial benzoic acid from PTA (pure terephthalic acid) process wastewater. The method includes following steps: (1), heating PTA process wastewater to 95-105 DEG C, and obtaining terephthalic acid solid and mixed liquid containing benzoic acid, cobalt and manganese by centrifugal separation; (2), cooling the mixed liquid containing benzoic acid, cobalt and manganese by a jacketed reactor, and filtering the mixed liquid after cooling by adopting a diaphragm plate-and-frame filter press to obtain a benzoic acid elementary product; (3), drying the benzoic acid elementary product by a belt-type dryer; (4), placing the benzoic acid elementary product after drying into a premelting kettle for heating to 100 DEG C to 110 DEG C for vacuum dehydration; (5), placing the benzoic acid elementary product after vacuum dehydration into a fractionating tower, heating and fusing to be in a liquid state, continuing to heat for vaporization, and cooling the product after vaporization by a condenser; and (6), inputting the product after condensation into a slicing machine, using the slicing machine to cool for flaking, and obtaining the industrial-level benzoic acid finished product. The method for separating and refining the industrial benzoic acid from the PTA process wastewater is high in recovery, low in energy consumption, capable of recycling heat, energy-saving and environment-friendly.

Description

technical field [0001] The invention discloses a method for separating and refining industrial benzoic acid from PTA process wastewater. Background technique [0002] The treatment of oxidation residues and waste water produced in the production process of terephthalic acid (PTA) has always been a difficult problem in environmental protection. In the process of PTA production, the waste water produced contains a large amount of benzoic acid, terephthalic acid and isophthalic acid. In addition to organic compounds such as cobalt and manganese salts, it also contains inorganic compounds such as cobalt and manganese salts. Among them, cobalt acetate and manganese acetate are catalysts in the production of terephthalic acid. After the catalyst is used for a period of time, its catalytic activity weakens and is discharged along with the beating wastewater. When treating wastewater and oxidation residues, its technical core includes the separation and purification of benzoic aci...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C63/06C07C51/42C07C63/26
CPCY02P20/50
Inventor 陈长征陈久永
Owner 江苏华旭环保股份有限公司
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