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Preparation method of zirconium sulfate

A technology of zirconium sulfate and sulfuric acid, applied in the direction of zirconium sulfate, etc., can solve the problems of difficult sodium removal, difficulty in filtration, low leaching rate, etc., and achieve the effects of environmental protection, avoiding harmful waste gas, and improving production efficiency

Inactive Publication Date: 2020-07-17
绵竹市金坤化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] (1) Both method 1 and method 2 use alkali fusion, and the raw material for alkali fusion is generally sodium hydroxide or sodium carbonate, which increases the subsequent sodium removal step and forms Na 2 [ZrO(SO 4 ) 2 ]·3H 2 The double salt of O is more difficult to remove sodium; (2) method 1 and method 2 both have alkali fusion steps, so it is necessary to increase the step of acid solution leaching. In method 1, sulfuric acid leaching is used, and the amount of sulfuric acid needs to be precisely controlled. Insufficient sulfuric acid, the Na in the transition material 2 ZrSiO 5 It is difficult to leaching, the leaching rate is low, and the silicic acid is not well condensed, it is difficult to filter, the sulfuric acid is too much, the acidity of the leachate is too high, it is difficult to evaporate, and it is easy to form silica gel during the evaporation process, and it is difficult to filter; in the second method, hydrochloric acid is used for leaching, which is easy to cause The production equipment is severely corroded; (3) method one requires recrystallization to obtain high-purity zirconium sulfate, while method two uses low-acid leaching and high-acid dissolution, and the product yield is low

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] Crush zircon sand into zircon sand fine powder with a particle size of less than 325 meshes, and react zircon sand fine powder with sulfuric acid at 0.5MPa and 200°C for 5 hours, wherein the mass ratio of zircon sand to sulfuric acid is 1:5.5 , the concentration of sulfuric acid is 70%; after the reaction is completed, cool to below 100°C, add water 5 times the mass of zircon sand for stirring and washing, then filter and collect the filtrate, add oxalic acid to the filtrate for complexation, add oxalic acid The mass is 3.5 times that of ferric oxide, the reaction temperature is 60°C, the reaction is 2h, and the obtained solution is crystallized to obtain zirconium sulfate.

Embodiment 2

[0023] Crush zircon sand into zircon sand fine powder with a particle size of less than 325 mesh, and react zircon sand fine powder with sulfuric acid at 0.5MPa and 210°C for 4 hours, wherein the mass ratio of zircon sand to sulfuric acid is 1:5.6 , the concentration of sulfuric acid is 68%; after the reaction is completed, cool to below 100°C, add water 10 times the mass of zircon sand for stirring and washing, then filter and collect the filtrate, add pyrophosphoric acid to the filtrate for complexation, coke The mass of phosphoric acid added was 2.6 times that of ferric oxide, the reaction temperature was 65° C., and the reaction was carried out for 2.5 hours. The obtained solution was crystallized to obtain zirconium sulfate.

Embodiment 3

[0025] Crush zircon sand into zircon sand fine powder with a particle size of less than 325 mesh, react zircon sand fine powder with sulfuric acid at 0.5MPa and 220°C for 3 hours, wherein the mass ratio of zircon sand to sulfuric acid is 1:5.7 , the concentration of sulfuric acid is 65%; after the reaction is completed, cool to below 100°C, add water 15 times the mass of the zircon sand for stirring and washing, then filter and collect the filtrate, add hydrochloric acid to the filtrate for complexation, add hydrochloric acid The mass is 1.8 times that of ferric oxide, the reaction temperature is 70°C, the reaction is 2.5h, and the obtained solution is crystallized to obtain zirconium sulfate.

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PUM

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Abstract

The invention discloses a zirconium sulfate preparation method, which comprises: carrying out a reaction on crushed zircon sand and sulfuric acid for 3-5 h under a pressurization heating condition, sequentially adding water to wash and filter after the reaction is completed, collecting a filtrate, removing impurities from the filtrate, and crystallizing an obtained zirconium sulfate solution to obtain zirconium sulfate. Zirconium sulfate is prepared by directly reacting zircon sand with sulfuric acid under the conditions of heating and pressurizing, alkali fusion is not adopted, sodium hydroxide or sodium carbonate is avoided, the step of removing sodium is omitted, and high-purity zirconium sulfate can be obtained only through one-time crystallization.

Description

technical field [0001] The invention belongs to the field of zirconium sulfate preparation, in particular to a method for preparing zirconium sulfate. Background technique [0002] Zirconium sulfate is an intermediate product used to prepare other zirconium compounds, and can also be sold as a finished product for rubber, papermaking, leather tanning and other industries. There are many ways to produce zirconium sulfate. The methods for producing zirconium sulfate from zircon are: (1) zircon → alkali fusion → water washingsulfuric acid leaching → ammonia precipitation → washing to remove sodium → sulfuric acid dissolutionevaporation crystallization → recrystallization → Zirconium sulfate products; (2) Zircon → alkali fusion → water washinghydrochloric acid leaching → hydrolysis → sulfuric acid dissolutioncrystallization → zirconium sulfate products. There are following disadvantages from the above two methods: [0003] (1) Both method 1 and method 2 use alkali ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01G25/06
CPCC01G25/06
Inventor 焦海坡黄伯璞
Owner 绵竹市金坤化工有限公司
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