Method of treating hexane diacid preparation waste liquid

An adipic acid and waste liquid technology, applied in natural water treatment, chemical instruments and methods, extraction water/sewage treatment, etc., can solve the problems of large gas discharge, easy coking of products, dark color of products, etc., to reduce losses, Avoid sublimation or decomposition, the effect of low processing cost

Inactive Publication Date: 2008-08-13
李强国
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Problems solved by technology

[0004] 1. In this process, NO 2 The absorption effect is affected by factors such as changes in the concentration of lye, changes in gas flow rate, and changes in gas temperature. These factors are likely to cause NO 2 A large amount of gas is discharged, polluting the air;
[0005] 2. This process needs to evaporate about 80% of the water in the adipic acid waste liquid, so the energy consumption is relatively high;
[0006] 3. The process requires a high temperature of 160°C to 180°C to decompose and produce NO 2 Gas, at high temperature, part of succinic acid, glutaric acid and adipic acid sublimate and run away, and part of triacids (adipic acid, glutaric acid and succinic acid) decompose, high energy consumption, easy loss, and easy coking of the product. The product is dark in color and poor in quality

Method used

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  • Method of treating hexane diacid preparation waste liquid

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Embodiment approach

[0029] A method for processing adipic acid production waste liquid, comprising the steps of:

[0030] (1), take the adipic acid production waste liquid of V volume and the ethyl acetate extraction agent of V volume, add in the extraction equipment 1 together, under normal temperature and pressure, carry out vibration extraction, then static, when organic phase and aqueous phase After layering, the aqueous phase flows out from the extraction device 1, which is called 1b, and the remaining extract containing triacids (adipic acid, glutaric acid and succinic acid) is called 1a;

[0031] (2), then weigh V volumes of adipic acid production waste liquid, pour it into the extraction equipment 2, and then pour into the extract 1a containing triacids (adipic acid, glutaric acid and succinic acid) in a certain proportion , under normal temperature and pressure, carry out vibration extraction, then stand still, when the organic phase and the water phase are separated, the water phase flo...

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Abstract

This invention provides a treatment method for waste liquid from adipic acid production with simple process, good effect and low cost. Said method comprises: (1) adding waste liquid from adipic acid production and the extraction agent of ethyl acetate with the same volume as the waste liquid in an extraction equipment, vibrating and extracting, and standing to stratify the water and organic item, and flowing out the water and the remained extract containing three acids (adipic acid, glutaric acid and succinic acid), (2) repeating above steps to extract, (3) distilling the three acids-bearing extract no longer to be treated, evaporating the extraction agent of ethyl acetate, recycling, cooling the remainder and molding to obtain the three acids, and (3) adding alkaline substance to the water no longer to be treated, adjusting its pH within a range of 7-8, and discharging or taking it as liquid fertilizer. The approach is an advanced and mature technology with low energy consumption and no pollution. The three acid obtained have good quality and high efficiency.

Description

technical field [0001] The invention relates to a method for processing industrial waste liquid, in particular, relates to a method for processing adipic acid production waste liquid. Background technique [0002] At present, the large-scale enterprises producing adipic acid in my country mainly include Liaoyang Petrochemical Group and Pingdingshan Shenma Group 66 Salt Company. The treatment methods of adipic acid production waste liquid produced by these two enterprises are basically the same: Put the waste liquid into an acid-resistant reaction kettle, heat it with steam to evaporate the water and dilute nitric acid in the production waste liquid; then add lime to neutralize the condensed water of water vapor and nitric acid, adjust the pH value to 7-8, Finally, discharge; in addition, add the waste adipic acid without water into the high-temperature reactor to pass heat conduction oil, and continue heating. When the temperature reaches 160 ° C ~ 180 ° C, the contained nitri...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C55/02C07C55/10C07C55/12C07C55/14C07C51/42C02F1/26C02F103/36
Inventor 李强国
Owner 李强国
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