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Method and system for carrying out automatic solid-liquid continuous washing and separation

An automatic, solvent-washing technology, applied in separation methods, chemical instruments and methods, filtration and separation, etc., can solve problems such as increasing energy consumption, increasing production costs of enterprises, and difficulty in washing

Inactive Publication Date: 2018-12-21
QINGHAI INST OF SALT LAKES OF CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, when the filter equipment is used to separate powder materials, it usually requires a lot of pressure, so the energy consumption is too high; in addition, when the filter equipment is small in size or slurry, it is easy to have a phenomenon of permeation, so the requirements for the filter membrane It is very high, which will increase the production cost of the enterprise; in addition, the water content of the powder material obtained after filtering by the filtration equipment is still high, and it is difficult to achieve complete separation of solid and liquid
When the centrifugal separator needs a high centrifugal speed for powder materials with low separation coefficients (such as graphene materials with small mass, small-sized nanomaterials, etc.), high-speed centrifuges are not only expensive, but also usually A refrigeration system is required, which will not only increase energy consumption, but also be limited by many product technical indicators
In addition, centrifugal separation and filtration separation generally use centrifuges, plate and frame filter presses, vacuum filters, etc. These filtration methods are all separated by solvent dispersion after centrifugation, that is, a one-pot separation method, such as Patents CN104307369A, CN103508473A, etc., are difficult to achieve continuous separation, and there are disadvantages such as high energy consumption, long time consumption, difficult washing, and difficulty in realizing automation and continuous production, which limits the industrial continuous and automatic production of powder materials
[0003] In addition, in the traditional production process of powder materials, due to the practical problem that powder materials are difficult to separate, it is difficult to wash the product after a solid-liquid separation, so there is often a problem of low purity of the obtained product

Method used

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  • Method and system for carrying out automatic solid-liquid continuous washing and separation

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preparation example Construction

[0040] In some embodiments, the preparation method specifically includes:

[0041] (1) placing the washing solvent in the first storage mechanism, and keeping the temperature of the washing solvent at the set temperature;

[0042] (2) Place the original solid slurry to be processed in the second storage mechanism, keep the temperature of the original solid slurry at a set temperature, and use an automatic flow control unit to input the washing solvent according to a set ratio In the original solid slurry, a first mixed liquid is obtained;

[0043] (3) input the first mixed liquid into the first separation or filtration assembly, and keep the temperature of the first separation or filtration assembly at the set temperature, and separate to obtain liquid phase and solid slurry;

[0044] (4) placing the liquid phase obtained in step (3) in the fourth storage mechanism, and keeping the temperature of the liquid phase at a set temperature;

[0045] (5) Place the solid slurry obta...

Embodiment 1

[0097] In this embodiment, the preparation of powdered magnesium hydroxide by magnesium chloride is taken as an example to describe the device and its usage method in the present invention.

[0098] 1. the solid content obtained by magnesium chloride and sodium hydroxide reaction is 10% reaction feed liquid (which contains magnesium hydroxide product and sodium chloride impurity, will contain sodium chloride impurity in the magnesium hydroxide product if not through washing ) enters the first ceramic membrane module 3 after being diluted with the washing solvent and slurry according to 5:1, wherein the solid slurry enters the third storage tank 4 through the solid discharge port, and the liquid enters the fourth storage tank through the liquid discharge port 5. The process can be operated at room temperature (25°C).

[0099] 2. Dilute the magnesium hydroxide slurry in the third storage tank 4 by 5 times with water, dissolve the sodium chloride in water, and continue to send th...

Embodiment 2

[0103] 1. the solid content obtained by reacting magnesium chloride and sodium hydroxide is 5% reaction feed liquid (which contains magnesium hydroxide product and sodium chloride impurity, if not through washing will contain sodium chloride impurity in the magnesium hydroxide product ) enters the first filter assembly through the metering pump, wherein the solid slurry enters the third storage tank 4 through the solid discharge port, and the liquid enters the fourth storage tank 5 through the liquid discharge port, and an automatic temperature control system is used to keep the raw material in the second The temperature of the storage tank 2, the first storage tank 1 of the washing solvent, the first filter assembly, the third storage tank 4, and the fourth storage tank 5 is 50°C;

[0104] 2. Dilute the magnesium hydroxide feed liquid in the third storage tank 4 with water 20 times, make the sodium chloride therein dissolve in water, and continue to send the diluted magnesium ...

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Abstract

The invention discloses a method and a system for carrying out automatic solid-liquid continuous washing and separation. The method comprises the following steps: inputting a washing solvent into a to-be-treated initial solid size by adopting an automatic flow control unit, thus obtaining a first mixed solution; inputting the first mixed solution into a separation or filter assembly, and separating, thus obtaining a liquid phase and a solid size; inputting the washing solvent into the solid size obtained through separation by adopting the automatic flow control unit, thus obtaining a second mixed solution; inputting the second mixed solution into a next separation or filter assembly, and separating again, thus obtaining the liquid phase and the solid size; repeating the operation for at least once, and testing the electrical conductivity or the pH (Potential of Hydrogen) value of the liquid phase which is obtained every time until the electrical conductivity or the pH value of the liquid phase is constant. According to the method disclosed by the invention, charging and discharging of the washing solvent and a powder-containing solid size can be controlled through a DSC (Dynamic Stability Control) system, continuous and automatic washing and solid-liquid separation of powder materials can be realized through programs such as a temperature control program of the system, and industrial automatic separation and washing can be easily realized.

Description

technical field [0001] The invention relates to a solid-liquid separation method, in particular to a continuous automatic solid-liquid continuous washing and separation method and system for powder materials, belonging to the technical field of solid-liquid separation. Background technique [0002] In recent years, with the continuous development of material technology, the material preparation process has also been continuously improved. Among them, washing and separation technology is a very important link in the material preparation process. Traditional solid-liquid separation devices for powder materials include centrifugal equipment such as centrifugal separators and filtering equipment such as centrifugal filters, vacuum filters, pressure filters, and plate-and-frame filters. These devices play a very critical role in the solid-liquid separation process in the preparation of powder materials. However, when the filter equipment is used to separate powder materials, it...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D37/00
CPCB01D37/00
Inventor 樊发英唐志雷邓小川张毅朱朝梁樊洁卿彬菊史一飞张文丁
Owner QINGHAI INST OF SALT LAKES OF CHINESE ACAD OF SCI
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