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Improved T acid wastewater extraction process and preparation method of modified naphthalene dispersant or naphthalene water reducer

A technology of naphthalene-based water reducer and naphthalene-based dispersant, which is applied in the direction of extraction water/sewage treatment, etc. It can solve the problem of reluctance to use, affect the dispersibility of products, affect the dispersibility of naphthalene-based dispersants or naphthalene-based water-reducers, etc. question

Inactive Publication Date: 2019-10-15
华颢控股(集团)有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] H-acid intermediates are extremely important raw materials in the synthesis of reactive dyes, acid dyes and other dyes. However, in the production process, T-acid wastewater and H-acid wastewater will be generated. The current treatment method is through traditional extraction methods. The organic matter is highly concentrated together, but because in the process of extraction and stripping, new sodium sulfate will still be entrained, and the content is relatively high, generally exceeding 15%. The use of naphthalene-based sulfonated compounds has brought great difficulties. Some people have tried to add them in the condensation reaction stage of naphthalene-based sulfonated compounds during the preparation of naphthalene-based dispersants or naphthalene-based water reducers, trying to make these organic compounds access to naphthalene-based dispersants. Naphthalene-based water reducer or naphthalene-based water reducer molecular structure, but without success, it affects the dispersion performance of naphthalene-based dispersant or naphthalene-based water-reducer. The fundamental reason is that during the condensation reaction, methylene can only condense in these On the amino group of the organic matter, this is equivalent to terminating the further condensation of the molecular chain of the naphthalene-based sulfonate, which will affect the normal condensation reaction of the naphthalene-based sulfonate, greatly reducing the molecular weight of the product, thereby seriously affecting the dispersion performance of the product
This has led to many manufacturers of naphthalene-based dispersants or naphthalene-based water reducers unwilling to use highly concentrated organic matter in wastewater provided by H-acid manufacturers.

Method used

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preparation example Construction

[0034] The present invention also provides a preparation method of a modified naphthalene-based dispersant or a naphthalene-based water reducer, comprising the following steps:

[0035] S1. Add 100-150 parts of naphthalene or methylnaphthalene to the reaction kettle, heat up to 130-170°C, and obtain reaction solution 1;

[0036] S2. Add 100 to 150 parts of concentrated sulfuric acid dropwise to the reaction solution 1, control the temperature to 130 to 170° C., after the dropwise addition is completed, carry out sulfonation reaction to obtain reactant 2;

[0037] S3. Add 50-150 parts of the waste T acid-alkaline liquid dropwise to the reactant 2, lower the temperature to 100-130° C., maintain the hydrolysis reaction, and obtain the reactant 3;

[0038] S4. Add 50-150 parts of 37% formaldehyde dropwise to the reactant three, control the temperature to 80-100°C, after the dropwise addition is completed, raise the temperature to 100-110°C to carry out the condensation reaction; ...

Embodiment 1

[0044] A kind of T acid waste water extraction process, comprises the steps:

[0045] S1. In the reactor, add 2800 parts of T-acid wastewater, adjust the pH of the system with 100 parts of concentrated sulfuric acid, and adjust the pH of the system to 1.5;

[0046] S2, add 3750 parts of extractant, mix, let stand;

[0047] S3. Separating the liquid containing inorganic salts and the waste T-acid complex, completing the extraction, and obtaining the waste T-acid complex;

[0048] S4, preparing 400 parts of stripping agent, adding 60 parts of stripping agent and water of the same amount to the waste T-acid complex, mixing, standing, and separating the liquid of sodium sulfate;

[0049] S5. Continue to add the remaining stripping agent, mix, and stand still to separate the waste T acid-base liquid with a sodium sulfate content of less than 10% and recover the extraction agent.

[0050] A preparation method of a modified naphthalene-based dispersant or a naphthalene-based water ...

Embodiment 2

[0057] A kind of T acid waste water extraction process, comprises the steps:

[0058] S1. In the reactor, add 2950 parts of T-acid waste water, adjust the pH of the system with 140 parts of concentrated sulfuric acid, and adjust the pH of the system to 1.4;

[0059] S2, add 3950 parts of extractant, mix, let stand;

[0060] S3. Separating the liquid containing inorganic salts and the waste T-acid complex, completing the extraction, and obtaining the waste T-acid complex;

[0061] S4, prepare 440 parts of stripping agent, add 65 parts of stripping agent and the same amount of water into the waste T-acid complex, mix, let stand, and separate the liquid of sodium sulfate;

[0062] S5. Continue to add the remaining stripping agent, mix, and stand still to separate the waste T acid-base liquid with a sodium sulfate content of less than 10% and recover the extraction agent.

[0063] A preparation method of a modified naphthalene-based dispersant or a naphthalene-based water reduce...

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PUM

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Abstract

The invention discloses an improved T acid wastewater extraction process and a preparation method of a modified naphthalene dispersant or naphthalene water reducer. Specifically, the T acid wastewaterextraction process uses concentrated sulfuric acid to adjust the pH value of T acid wastewater, also utilizes an extractant to extract a waste T acid complex, and then performs back extraction through a back-extractant, thus obtaining waste T acid alkaline liquid with a sodium sulfate content of less than 10% and a recovered extractant. The recovered extractant can be repeatedly used for T acid wastewater extraction process, and the waste T acid alkaline liquid can be used for preparation of the undermentioned modified naphthalene dispersant or naphthalene water reducer. The preparation method of the modified naphthalene dispersant or naphthalene water reducer includes: subjecting naphthalene or methylnaphthalene to sulfonation reaction, adding the waste T acid alkaline liquid for hydrolysis reaction, and adding formaldehyde dropwise for condensation reaction, thus finally obtaining a modified naphthalene dispersant or naphthalene water reducer liquid product with a solid content of 30-50%.

Description

technical field [0001] The invention relates to the technical field of wastewater treatment, in particular to an improved T-acid wastewater extraction process and a preparation method for a modified naphthalene-based dispersant or a naphthalene-based water reducer. Background technique [0002] H-acid intermediates are extremely important raw materials in the synthesis of reactive dyes, acid dyes and other dyes. However, in the production process, T-acid wastewater and H-acid wastewater will be generated. The current treatment method is through traditional extraction methods. The organic matter is highly concentrated together, but because in the process of extraction and stripping, new sodium sulfate will still be entrained, and the content is relatively high, generally exceeding 15%. The use of naphthalene-based sulfonated compounds has brought great difficulties. Some people have tried to add them in the condensation reaction stage of naphthalene-based sulfonated compounds...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C04B24/22C02F1/26C08G16/02C04B103/30C04B103/40
CPCC04B24/226C02F1/26C08G16/0237C04B2103/302C04B2103/408
Inventor 高俊徐蔚徐少华
Owner 华颢控股(集团)有限公司
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