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Method for preparing trihydrated magnesium carbonate by using continuous crystallization process

A technology of magnesium carbonate trihydrate and crystallization method, applied in directions such as magnesium carbonate, solution crystallization, etc., can solve the problem of difficult to meet the continuous crystallization production of magnesium carbonate trihydrate, disadvantageous large-scale production of magnesium carbonate trihydrate, and the particle size and particle size distribution of easily broken products. and other problems, to achieve the effect of continuous aging, good economic benefits and good crystal shape

Inactive Publication Date: 2011-09-21
INST OF PROCESS ENG CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0025] At present, the processes for preparing magnesium carbonate trihydrate in literature and production are all batch crystallization processes, which have a low degree of automation, small capacity of a single set of equipment, long reaction time, lack of continuity in production before and after, and production is easily affected by human factors, resulting in product quality. Unstable phenomenon, not conducive to large-scale production of magnesium carbonate trihydrate
The continuous method crystallization process has the advantages of high production capacity, high degree of automation, stable product quality, etc., but because magnesium carbonate trihydrate has its special crystallization process characteristics and product quality requirements, such as the characteristics of reaction crystallization, there are certain conditions in the crystallization process. The induction period, the rod-shaped product is easily broken during the crystallization process and affects the particle size and particle size distribution of the product, and the concentration of remaining raw materials in the mother liquor after crystallization is relatively high, making it difficult for the traditional continuous crystallization process to meet the needs of continuous crystallization of magnesium carbonate trihydrate.

Method used

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  • Method for preparing trihydrated magnesium carbonate by using continuous crystallization process
  • Method for preparing trihydrated magnesium carbonate by using continuous crystallization process
  • Method for preparing trihydrated magnesium carbonate by using continuous crystallization process

Examples

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Effect test

Embodiment 1

[0050] Add deionized water into magnesium chloride brine and ammonium carbonate solution respectively to prepare 0.5mol / L magnesium chloride and ammonium carbonate solution. Add 2.5kg of magnesium carbonate trihydrate seed crystals to the continuous crystallization kettle, heat the crystallization kettle to keep its solution at 10°C, start the stirring device, and start the continuous feeding of magnesium chloride solution and ammonium carbonate solution. The flow rate of the two materials is 6.7 L / min, control the stoichiometric ratio of adding magnesium chloride and ammonium carbonate to be 1:1.1, and control the pH value of the crystallization solution between 7.0 and 7.5, and the average residence time is 3 hours. When the volume of the magma in the reactor reaches the effective volume (1600L), the magma starts to flow out, and the outflow flow of the magma is the sum of the two feeds. The outflowing crystal slurry is pumped to a continuous settler for aging, and the avera...

Embodiment 2

[0052] Add deionized water into magnesium chloride brine and ammonium carbonate solution respectively to prepare 3.0 mol / L magnesium chloride and ammonium carbonate solution. Add 1.0 kg of magnesium carbonate trihydrate seed crystals to the continuous crystallization kettle, heat the crystallization kettle to keep the solution at 50°C, start the stirring device, and start the continuous feeding of the magnesium chloride solution and the ammonium carbonate solution, and the flow rate of the two materials is 3L / min, control the stoichiometric ratio of adding magnesium chloride and ammonium carbonate to 1:1.2, and control the pH value of the crystallization solution between 9.5 and 10.0, and the average residence time is 0.5 hours. When the volume of the magma in the reactor reaches the effective volume (1600L), the magma starts to flow out, and the outflow flow of the magma is the sum of the two feeds. The outflowing crystal slurry is pumped to a continuous settler for aging, a...

Embodiment 3

[0054] Add deionized water to magnesium chloride brine and ammonium carbonate solution respectively to prepare 1.0 mol / L magnesium chloride and ammonium carbonate solution. Add 1.0kg of magnesium carbonate trihydrate seed crystals to the continuous crystallization kettle, heat the crystallization kettle to keep the solution at 40°C, start the stirring device, and start the continuous feeding of magnesium chloride solution and ammonium carbonate solution, the flow rate of the two materials is 5L / min, control the stoichiometric ratio of adding magnesium chloride and ammonium carbonate to 1:1.15, and control the pH value of the crystallization solution between 8.0 and 9.0, and the average residence time is 1 hour. When the volume of the magma in the reactor reaches the effective volume (1600L), the magma starts to flow out, and the outflow flow of the magma is the sum of the two feeds. The outflowing crystal slurry is pumped to a continuous settler for aging, and the average res...

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Abstract

The invention belongs to the technical field of salt chemical industrial production, concretely, the invention relates to a method for preparing trihydrated magnesium carbonate by a using continuous crystallization process. The technical schemes of the present invention comprises: selecting high concentration magnesium chloride or high ratio of magnesium to lithium brine, ammonium carbonate as raw materials, adding into a continuous crystallizer for crystallizing, adding a crude product of trihydrated magnesium carbonate obtained by crystaling into an aging device for aging, obtaining a trihydrated magnesium carbonate crystal with good form and high purity for condition for providing conditions to produce high purity magnesium oxide. According to the method of the present invention, continuous crystallization in a process of producing trihydrated magnesium carbonate can be realized, the stability and automation degree of the crystallization in the process of producing trihydrated magnesium carbonate can be effectively raised, and the quality of products is increased as well as the production cost is reduced.

Description

technical field [0001] The invention belongs to the technical field of salt chemical production. Specifically, the invention relates to a method for preparing magnesium carbonate trihydrate by using a continuous crystallization method. Background technique [0002] my country has vast salt lake resources in Qinghai, Tibet, Xinjiang and other regions, and the salt lakes are rich in potassium, magnesium, lithium and other resources. At present, the area mainly produces potash fertilizer, and a large amount of brine containing magnesium chloride and lithium chloride is discharged during the production process of potash fertilizer. This part of brine has not been effectively utilized, resulting in the waste of magnesium and lithium resources, and also the depletion of potassium resources and serious environmental pollution. With the development of the national economy, the demand for magnesium products in the domestic market is also increasing, but high-end magnesium products s...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01F5/24B01D9/02
Inventor 李志宝王勇
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI
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