Method for extracting potassium sodium salts from m-aminophenol alkali fusion wastewater

A technology of m-aminophenol alkali and aminophenol alkali, which is applied in the field of extracting potassium and sodium salts, can solve the problems of low utilization value of recovered salt, low purity, high consumption of expensive solvents, etc., and achieves simple and easy extraction process and high extraction recovery rate , the effect of high product purity

Pending Publication Date: 2020-12-04
HEBEI JIANXIN CHEM IND CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Common methods for extracting salt from wastewater such as: evaporation crystallization, ion exchange, electrodialysis, RO reverse osmosis, and electrosorption. The types of salt obtained by such methods are complex and low in purity, and it is difficult to separate and purify a single type of salt, resulting in Recovered salt has low utilization value, and has disadvantages such as low efficiency, high energy consumption, and high cost
In the actual industrial development process, high-purity potassium and sodium salts are often required. The Chinese patent application number 201710436809.2 discloses a separation system and a separation method for sodium and potassium salts. This method passes through crystallization and separation equipment, heat preservation and sedimentation equipment, cooling Crystallization equipment and centrifugal equ

Method used

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Examples

Experimental program
Comparison scheme
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Example Embodiment

[0031] Example 1

[0032] The method for separating and extracting potassium and sodium from m-aminophenol alkali melting wastewater comprises the following steps:

[0033] The solid impurities and oily substances in the wastewater from alkali melting of m-aminophenol were removed by filtration, and the potassium and sodium contents were detected by flame photometer. Add 57.5g of fluosilicic acid with the content of 12% into the reaction bottle, stir at 20℃ and slowly drop 100g; of m-aminophenol alkali melting wastewater; Keeping the temperature at 20℃ and stirring for 20min;; After the reaction, the above system was filtered to obtain crude potassium fluosilicate, the filter cake was added into 50g of water, stirred evenly, and 1g of potassium chloride was added at 20℃, and the reaction temperature was 20℃ for 20min. Filtering and drying at 120℃ to obtain 10.4g of potassium fluosilicate product with purity over 99%, and the recovery rate of potassium salt over 95%; At the tempera...

Example Embodiment

[0038] Example 2

[0039] The method for separating and extracting potassium and sodium from m-aminophenol alkali melting wastewater comprises the following steps:

[0040] The solid impurities and oily substances in the wastewater from alkali melting of m-aminophenol were removed by filtration, and the potassium and sodium contents were detected by flame photometer. Add 39.4g of fluosilicic acid with 15% content into the reaction bottle, stir at 40℃ and slowly drop 100g; of m-aminophenol alkali melting wastewater; Keeping the temperature at 40℃ and stirring for 10min;; After the reaction, the above system was filtered to obtain crude potassium fluosilicate, the filter cake was added into 70g of water, stirred evenly, and 0.9g of potassium chloride was added at 40℃, and stirred for 10min at 40℃. Filtering and drying at 120℃ to obtain 9.2g potassium fluosilicate product with purity above 99%, and the recovery rate of potassium salt is above 95%; At 40℃, 91.2g of fluosilicic acid wi...

Example Embodiment

[0045] Example 3:

[0046] A method for separating and extracting potassium and sodium from m-aminophenol alkali melting wastewater comprises the following steps:

[0047]The solid impurities and oily substances in the wastewater from alkali melting of m-aminophenol were removed by filtration, and the potassium and sodium contents were detected by flame photometer. 18.93g of fluosilicic acid with the content of 35% was added into the reaction flask, stirred at 50℃ and slowly dropped into 100g; of m-aminophenol alkali melting wastewater; Keeping the temperature at 50℃ and stirring for 5min;; After the reaction, the above system was filtered to obtain crude potassium fluosilicate, the filter cake was added into 60g of water, stirred evenly, and then 0.85g of potassium chloride was added at 50℃ and stirred for 5min at 50℃. Filtering and drying at 120℃ to obtain 9.4g of potassium fluosilicate product with purity above 99%, and the recovery rate of potassium salt is above 95%; At 50℃, ...

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Abstract

The invention relates to a method for extracting potassium sodium salts from m-aminophenol alkali fusion wastewater, wherein the method comprises the steps: filtering to remove solid impurities and oily substances in the wastewater, and detecting the potassium and sodium content in the wastewater; adding a fluosilicic acid solution with the content of 10-35% into a reaction bottle, slowly dropwiseadding m-aminophenol alkali fusion wastewater while stirring at the temperature of 20-50 DEG C, and after dropwise adding is finished, carrying out heat-preservation stirring reaction for 5-30 min; filtering to obtain a potassium fluosilicate crude product, adding a filter cake into water, uniformly stirring, adding potassium chloride at the temperature of 20-50 DEG C, and carrying out stirring reaction for 5-30 min; filtering, and drying a filter cake at the temperature of 100-120 DEG C to obtain a potassium fluosilicate finished product; at the temperature of 20-50 DEG C, adding fluosilicicacid with the content of 10-35% into another reaction bottle, and continuously and slowly dropwise adding wastewater mother liquor with a potassium salt extracted into the reaction bottle for stirring reaction for 5-30 min; and filtering, adding pure water into the filter cake, pulping and washing until the pH value is equal to 7, filtering, and drying the filter cake at the temperature of 100-120 DEG C to obtain sodium fluosilicate. According to the method, the potassium sodium salt in the m-aminophenol alkali fusion wastewater is sequentially extracted by utilizing fluosilicic acid, and theobtained potassium fluosilicate and sodium fluosilicate are high in purity and high in recovery rate.

Description

technical field [0001] The invention relates to a method for extracting potassium and sodium salts from m-aminophenol alkali-melted wastewater, and belongs to the technical field of industrial wastewater treatment. Background technique [0002] Recycling of waste is a social requirement to recover useful substances and energy from waste by adopting various engineering techniques and management measures to realize resource recycling and avoid waste of resources. In recent years, with the development of human society, wastes have been increasing and various resources have been wasted. The recycling of waste water and waste needs to attract people's attention. [0003] As a dye intermediate and pharmaceutical intermediate, m-aminophenol is widely used in fine chemicals such as dyes, functional dyes, medicines, and pesticides, such as black coupler ODB in thermosensitive dyes, anti-tuberculosis drugs (p-aminosalicylic acid) , fungicides (fungalamine and fluoroamide) and develop...

Claims

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Application Information

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IPC IPC(8): C02F9/04C01B33/10C02F103/34
CPCC02F1/001C02F1/583C01B33/103C02F2103/34C01P2006/80
Inventor 刘佳伟朱秀全刘敬张静李文慧
Owner HEBEI JIANXIN CHEM IND CO LTD
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