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Treatment process for wastewater from N-(Phosphonomethyl)iminodiacetic acid production

A technology for producing wastewater and treatment methods, which is applied in natural water treatment, heating water/sewage treatment, neutralized water/sewage treatment, etc. It can solve the problems of incomplete combustion, polluted waste gas, and large treatment costs, and reduce treatment costs. Cost, Environmentally Friendly Effects

Inactive Publication Date: 2009-05-13
SICHUAN BEIER CHEM GROUP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] 1) Incineration of waste water with fuel, the incineration operation is cumbersome, unstable, and the treatment cost is high;
[0008] 2) In the later stage of incineration, due to the sodium chloride in the waste water, the salt is easy to crystallize and accumulate on the wall of the incinerator. If the operation is not good, there is a danger of frying the furnace;
[0009] 3) Due to the incomplete combustion during the incineration process, the second polluted waste gas is generated. It is necessary to build a set of tail gas treatment system, and after treatment, it will be discharged up to the standard.
[0010] However, if the diglyphosate wastewater is treated by the above three methods to reach the discharge standard, a large treatment cost is required, which greatly increases the treatment cost of the diglyphosate production wastewater.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] The wastewater produced by bisglyphosate is pumped into a set of three-effect evaporator with a treatment capacity of 400 cubic meters per day at a rate of 16 cubic meters per hour, and the vacuum system is started (vacuum degree is 0.05-0.08MPa) and steam ( The vapor pressure is 0.1~0.4MPa) heating and evaporating the waste water produced by bisglyphosate, the amount of evaporated water is 9 cubic meters per hour, the evaporated water is put into a receiving pool, and the concentrated solution containing sodium chloride pumped out by the three-effect evaporator enters the crystallizer, After the salt crystallizes out, centrifuge to separate 1830kg / hour of sodium chloride wet material with a sodium chloride content of 87-91% and about 5 cubic meters / hour of separation liquid; about 5 cubic meters / hour of separation liquid is pumped Put into a solidification tank, add 200kg / hour curing agent (Chengjie Wi-4) to make it solidify, then move into a separator for solid-liquid ...

Embodiment 2

[0028] The wastewater produced by bisglyphosate is pumped into a set of three-effect evaporator with a treatment capacity of 400 cubic meters per day at a rate of 8 cubic meters per hour, and the vacuum system is started (vacuum degree is 0.05-0.08MPa) and steam ( The steam pressure is 0.1~0.4MPa) heating and evaporating the waste water produced by diglyphosate, the evaporation water volume is 4.5 cubic meters per hour, the evaporated water is put into a receiving pool, and the concentrated solution containing sodium chloride pumped out by the three-effect evaporator enters the crystallizer, After the salt crystallizes out, centrifuge to separate 930kg / hour of sodium chloride wet material with a sodium chloride content of 87-91% and about 2.6 cubic meters / hour of separation liquid; about 2.6 cubic meters / hour of separation liquid is pumped Put into a curing pool, add 100kg / hour curing agent (Chengjie Wi-4) to make it solidify, then move into a separator for solid-liquid separat...

Embodiment 3

[0030] The wastewater produced by bisglyphosate is pumped into a set of three-effect evaporator with a treatment capacity of 400 cubic meters per day at a rate of 12 cubic meters per hour, and the vacuum system is started (vacuum degree is 0.05-0.08MPa) and steam ( The steam pressure is 0.1~0.4MPa) heating and evaporating the wastewater produced by diglyphosate, the evaporated water volume is 6.7 cubic meters, and the evaporated water is put into a receiving pool, and the concentrated solution containing sodium chloride pumped out by the three-effect evaporator enters the crystallizer, and waits for the salt to crystallize After being discharged, it is centrifuged to separate 1340kg / hour of sodium chloride wet material with a sodium chloride content of 87-91% and a separation liquid of about 3.7 cubic meters / hour; the separation liquid is about 3.7 cubic meters / hour and is pumped into a solidification In the pond, add 150kg / hour curing agent (Chengjie Wi-4) to make it solidify,...

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PUM

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Abstract

The invention discloses a method for treating PMIDA (N-(phosphonomethyl)iminodiacetic acid) production wastewater, which comprises the following steps: 1) the PMIDA production wastewater is sent into equipment with a compound evaporator and a vacuum system, and is separated into a saturated concentrated solution containing sodium chloride and evaporable water at a steam pressure of between 0.1 and 0.4MPa and a vacuum degree of between 0.05 and 0.08MPa; the concentrated solution containing the sodium chloride is cooled to crystallize the sodium chloride; and the solid-liquid separation is performed; 2) separating medium is sent into a curing container, a curing agent is added, and innoxious solid mud and a filtrate are obtained after the washing and filtration; 3) after the evaporable water and the filtrate are mixed, a neutralizing agent is used to adjust the pH value to between 6 and 8; 4) an oxidant is added in neutralized wastewater for oxidation; and 5) a treated oxidized liquid is aerated and then enters the prior biochemical system to obtain treated water. The method can greatly reduce the treatment cost for the PMIDA production wastewater, can also extract partial useful constituents in the PMIDA production wastewater, can be recycled, and is favorable for the environmental protection.

Description

Technical field: [0001] The invention relates to a treatment method of chemical production wastewater, in particular to a treatment method of diglyphosate production wastewater. Background technique: [0002] In the production process of using iminodiacetonitrile or iminodiacetic acid as raw material, alkali hydrolysis to synthesize iminodiacetic acid sodium salt, and then phosphonoformylation reaction to synthesize diglyphosate, the separated aqueous solution after the solid product of diglyphosate is separated , which is the waste water from the production of bis-glyphosate. Diglyphosate production wastewater contains 05-5% diglyphosate, 1-7% HCl, 0.5-5% phosphorous acid, 0.5-3% formaldehyde, 8-18% sodium chloride and the like. The waste water will pollute the environment due to direct discharge, and waste water treatment is required. [0003] There are the following three methods for the treatment of wastewater from the production of diglyphosate in the past: [0004] ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/14C02F1/04C02F1/66C02F1/72C02F3/30C01D3/04C02F103/36
Inventor 王国成崔卫东杨华青卫平李柱全
Owner SICHUAN BEIER CHEM GROUP
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