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A kind of waste salt prepares the method for sodium carbonate by-product potassium sulfate, ammonium sulfate and ammonium chloride

A sodium carbonate and potassium sulfate technology, applied in the field of potassium sulfate, ammonium sulfate and ammonium chloride, waste salt purification treatment and preparation of sodium carbonate, can solve the problem of unavailable quality, high sodium sulfate and sodium chloride products, process energy consumption Advanced problems, to achieve significant economic and environmental benefits, process cleaning, process section effect

Active Publication Date: 2022-03-04
INST OF PROCESS ENG CHINESE ACAD OF SCI +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0002] At present, the output of chemical waste salt with sodium chloride and sodium sulfate as the main components is huge, and the treatment cost is high, and the high disposal cost has greatly increased the production and operation costs of related enterprises, and greatly restricted the technology of related enterprises. Upgrading and Sustainability
[0003] At present, the conventional disposal method of chemical waste salt is mainly to separate sodium sulfate and sodium chloride, mainly including salt-nitration separation method and nanofiltration separation method. Salt-nitration separation method is divided into thermal method and cold method. The circulation volume is large, the energy consumption is high, and the obtained products sodium sulfate and sodium chloride are of poor quality, low value, and poor market absorption capacity
The nanofiltration separation method can separate sodium chloride and sodium sulfate to a certain extent, but it cannot achieve complete separation of the two ions, so high-quality sodium sulfate and sodium chloride products cannot be obtained, and the process consumes a lot of energy. economy
In addition, sodium sulfate and sodium chloride are mainly upstream raw materials in the chemical industry. As by-products of solid waste treatment, due to the lack of relevant standards, the market acceptance is low and the market absorption capacity is limited. Most of them are stockpiled. As a soluble salt, it poses a serious threat to the environment

Method used

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  • A kind of waste salt prepares the method for sodium carbonate by-product potassium sulfate, ammonium sulfate and ammonium chloride
  • A kind of waste salt prepares the method for sodium carbonate by-product potassium sulfate, ammonium sulfate and ammonium chloride
  • A kind of waste salt prepares the method for sodium carbonate by-product potassium sulfate, ammonium sulfate and ammonium chloride

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Embodiment 1

[0043] Present embodiment provides a kind of method that waste salt prepares sodium carbonate by-product potassium sulfate, ammonium sulfate and ammonium chloride, and the process flow chart of described method is as follows figure 1 shown.

[0044] The method comprises the steps of:

[0045] (1) Mix the waste salt with the potassium removal solution obtained in step (3) (the liquid-solid ratio of fresh water to the waste salt is 1.8:1 when pulping for the first time), and stir at 90°C for pulping, stirring After reacting for 30 minutes, the slurry is separated by a cyclone, and the separated dilute phase slurry is subjected to the first solid-liquid separation to obtain insoluble organic matter and treatment liquid, and the separated dense phase slurry is subjected to the second solid-liquid separation to obtain the prefabricated Salt and treatment solution; the obtained prefabricated salt enters the preparation process of sodium carbonate and ammonium salt for treatment, th...

Embodiment 2

[0051] Present embodiment provides a kind of method that waste salt prepares sodium carbonate by-product potassium sulfate, ammonium sulfate and ammonium chloride, described method comprises the following steps:

[0052] (1) Mix the waste salt with the potassium removal solution obtained in step (3) (the liquid-solid ratio of fresh water to the waste salt is 2.5:1 during the first pulping), and stir at 85°C for pulping , after stirring and reacting for 60 minutes, the slurry is separated by a cyclone, and the separated dilute phase slurry is subjected to the first solid-liquid separation to obtain insoluble organic matter and treatment liquid, and the separated dense phase slurry is subjected to the second solid-liquid separation , to obtain prefabricated salt and treatment solution; the obtained prefabricated salt enters the preparation process of sodium carbonate and ammonium salt for treatment, the treatment solution enters the next process, and the insoluble organic matter ...

Embodiment 3

[0058] Present embodiment provides a kind of method that waste salt prepares sodium carbonate by-product potassium sulfate, ammonium sulfate and ammonium chloride, described method comprises the following steps:

[0059] (1) Mix the waste salt with the potassium removal solution obtained in step (3) (the liquid-solid ratio of fresh water to the waste salt is 2.0:1 when pulping for the first time), and stir at 85°C for pulping, stirring After reacting for 60 minutes, the materials are separated by a cyclone, and the separated dilute phase slurry is subjected to the first solid-liquid separation to obtain insoluble organic matter and treatment liquid, and the separated dense phase slurry is subjected to the second solid-liquid separation to obtain prefabricated salt and treatment solution; the obtained prefabricated salt enters the preparation process of sodium carbonate and ammonium salt for treatment, and the treatment solution enters the next process, and the insoluble organic...

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Abstract

The invention provides a method for preparing sodium carbonate by-product potassium sulfate, ammonium sulfate and ammonium chloride from waste salt. The method separates waste salt after pulping to obtain dilute phase slurry and dense phase slurry; The dilute phase slurry and the dense phase slurry are subjected to solid-liquid separation respectively to obtain insoluble organic matter, prefabricated salt and treatment liquid; the prefabricated salt enters the preparation process of sodium carbonate and ammonium salt for treatment to obtain sodium carbonate, ammonium sulfate and chloride ammonium chloride; the obtained treatment solution is oxidized to obtain a purification solution; when K in the purification solution + After the concentration reaches the preset value, precipitation treatment is carried out to obtain potassium-containing precipitate and potassium-removing solution; the potassium-containing precipitate enters the potassium sulfate preparation process; and the potassium-removing solution is returned to the pulping step for recycling. The method has clean process, simple process and low cost, the utilization rate of sodium is not less than 90.8%, the purity of sodium carbonate is not less than 97wt%, and the purity of potassium sulfate, ammonium sulfate and ammonium chloride obtained can meet certain requirements for use.

Description

technical field [0001] The invention belongs to the technical field of chemical engineering and environmental protection, and relates to a method for preparing sodium carbonate by-product potassium sulfate, ammonium sulfate and ammonium chloride from salt, in particular to a waste salt purification treatment and preparation of sodium carbonate, potassium sulfate, ammonium sulfate and ammonium chloride ammonium method. Background technique [0002] At present, the output of chemical waste salt with sodium chloride and sodium sulfate as the main components is huge, and the treatment cost is high, and the high disposal cost has greatly increased the production and operation costs of related enterprises, and greatly restricted the technology of related enterprises. Upgrading and sustainable development. [0003] At present, the conventional disposal method of chemical waste salt is mainly to separate sodium sulfate and sodium chloride, mainly including salt-nitration separation...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01D7/00C01C1/16C01C1/24C01D5/00
CPCC01D7/00C01C1/164C01C1/24C01D5/00C01P2006/80
Inventor 张洋范兵强张贺东申长帅郑诗礼曹宏斌陈沛松
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI