Granularity-controllable magnesium hydroxide reaction crystallization apparatus and process

A technology of reactive crystallization and magnesium hydroxide, which is applied in the directions of magnesium hydroxide, general layout of crystallization equipment, and crystallization separation, etc., can solve the problems of wide particle size distribution, difficult filtration, small addition amount, etc., and achieve the effect of narrow particle size distribution.

Active Publication Date: 2017-05-31
HEBEI UNIVERSITY OF SCIENCE AND TECHNOLOGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The product obtained by the ammonia method has high purity and large particle size, but there are air and water pollution in the production process, and the ammonia distillation operation is complicated and the cost is high.
The sodium hydroxide method can produce high-purity magnesium hydroxide products. If combined with the combined alkali production process, zero discharge of wastewater can be achieved and production costs can be effectively reduced; however, due to the strong alkalinity of sodium hydroxide, the reaction rate is too fast, The crystallization process is difficult to control, resulting in problems such as small particle size, wide particle size distribution, and difficulty in filtration and washing of the product obtained by reaction crystallization;
[0005] Chinese patent CN103043689A reports a device and process for preparing magnesium hydroxide by sodium hydroxide method. The supergravity reaction device is used to prepare nanoscale magnesium hydroxide products. The advantage of this method is that magnesium hydroxide products of 7-17 nanometers can be obtained , but the particle size of the product is too small, it is difficult to filter, and the specific surface area is large. It is used as a flame retardant in a small amount, and the power consumption in the production process is high.

Method used

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  • Granularity-controllable magnesium hydroxide reaction crystallization apparatus and process
  • Granularity-controllable magnesium hydroxide reaction crystallization apparatus and process
  • Granularity-controllable magnesium hydroxide reaction crystallization apparatus and process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037]The reaction crystallization device is composed of three stages of above-mentioned magnesium hydroxide reaction crystallizers (1). The crystallizer stirring blade (7) adopts 2 layers of down-pressing type propeller blades; a longitudinal partition (6) is installed between the jacketed kettle body (4) and the guide tube (5); the magnesium chloride feeding pipe (9) The outlet of the sodium hydroxide feed pipe (10) is located outside the guide tube (5), and the height of the nozzle is located at 20 cm above the lower edge of the guide tube (5), respectively arranged on the two sides of the longitudinal partition (6). Side; the diameter of the diversion cylinder (5) is 0.4 times of the inner diameter of the jacketed still body (4), and the lower edge of the diversion cylinder (5) is 15cm away from the bottom of the jacketed still body (4).

[0038] Add a sodium chloride solution with a mass concentration of 15% in each reaction crystallizer (1) as the reaction crystallizatio...

Embodiment 2

[0042] A reaction crystallization device is composed of six stages of above-mentioned magnesium hydroxide reaction crystallizers (1). The crystallizer stirring paddle (7) adopts 3 layers of down-pressing type propeller blades. A vertical partition (6) is installed between the jacketed still body (4) and the guide tube (5) of the first, second, and third-stage reaction crystallizers; the magnesium chloride feed pipe (9) mouth and the sodium hydroxide feed The mouths of the pipes (10) are all located outside the guide tube (5), and the nozzle heights are all located at 5 cm above the lower edge of the guide tube (5), and are respectively arranged on both sides of the longitudinal partition (6); the guide tube (5) ) diameter is 0.5 times of the inner diameter of the jacketed still body (4), and the lower edge of the draft tube (5) is 20cm away from the bottom of the jacketed still body (4). In the jacketed still body (4) of the 4th, 5th, and 6th stage reaction crystallizers, lon...

Embodiment 3

[0047] A reaction crystallization device is formed by adopting five stages of above-mentioned magnesium hydroxide reaction crystallizers (1). The crystallizer stirring paddle (7) adopts 3 layers of down-pressing type propeller blades. In the jacketed still body (4) of the 1st, 2nd, and 3rd stage reaction crystallizers, longitudinal partitions (6) are not installed, and the sodium hydroxide feed pipe (10) mouth is located in the guide tube (5). 5 cm below the upper edge of the flow tube (5); the magnesium chloride feed pipe (9) mouth is located outside the flow guide tube (5), 30 cm above the lower edge of the flow guide tube (5); the diameter of the flow guide tube (5) is jacketed 0.7 times of the inner diameter of the still body (4), the lower edge of the draft tube (5) is 40cm away from the bottom of the jacketed still body (4). Install vertical partition (6) between the jacketed still body (4) of the 4th, 5th grade reaction crystallizer and guide tube (5); Magnesium chlori...

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Abstract

The invention discloses a granularity-controllable magnesium hydroxide reaction crystallization apparatus and process. The reaction crystallization apparatus consists of a reaction crystallizer (1), a conveying pump (2) and a pipeline (3). The reaction crystallizer (1) comprises a jacket-type kettle body (4), a guide barrel (5), a longitudinal separation plate (6), a stirring paddle (7), an electric stirrer (8), a magnesium chloride feeding pipe (9), a sodium hydroxide feeding pipe (10), a feed distributor (11), a magnesium hydroxide discharging pipe (12) and a magnesium hydroxide feeding pipe (13). The invention also provides the magnesium hydroxide reaction crystallization process. By utilizing the apparatus and the process provided by the invention, the granularity-controllable production of the magnesium hydroxide can be realized, the magnesium hydroxide with different granularities can be prepared, and the requirements of different users on the granularity of a magnesium hydroxide product can be met. The granularity-controllable magnesium hydroxide reaction crystallization apparatus and process have the advantages of flexibility and adjustability in product granularity and narrow granularity distribution.

Description

technical field [0001] The invention belongs to the technical field of inorganic chemical industry, and relates to a reaction crystallization device and process of magnesium hydroxide with controllable particle size, in particular to a reaction crystallization device and process for synthesizing magnesium hydroxide with different particle sizes by using magnesium chloride and sodium hydroxide as raw materials. Background technique [0002] Magnesium hydroxide is an important multifunctional inorganic powder material, which can be used as a green inorganic flame retardant, flue gas desulfurizer, acid waste water neutralizer, water heavy metal remover, etc. It is used as an anti-acid in the pharmaceutical industry agents, laxatives; [0003] At present, the main production methods of magnesium hydroxide products include two categories, one is to use natural brucite to directly produce magnesium hydroxide through crushing and removing impurities; the other is to produce magnesi...

Claims

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Application Information

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IPC IPC(8): C01F5/22B01D9/02
CPCB01D9/0031B01D9/004B01D9/005B01D9/0059B01D2009/0086C01F5/22C01P2004/61
Inventor 刘宝树胡永琪刘润静孙华
Owner HEBEI UNIVERSITY OF SCIENCE AND TECHNOLOGY
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