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Method for preparing aluminum sulfate from aluminum-containing acid treatment solution

An acid treatment, aluminum sulfate technology, applied in aluminum sulfate, aluminum sulfur compounds, chemical instruments and methods, etc., can solve the problems of high process energy consumption, poor economy, single product, etc., achieve high purity, meet market needs, and The effect of industrial application value

Active Publication Date: 2021-06-29
CHNA ENERGY INVESTMENT CORP LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the product of extracting aluminum from fly ash is single, the process energy consumption is high, and the economy is poor

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment approach

[0043] According to a preferred embodiment of the present invention, preferably, the mass concentration of the concentrated sulfuric acid is 80-98%.

[0044] According to a preferred embodiment of the present invention, the volume ratio of the concentrated sulfuric acid to the gel filtrate is (0.1-2):1, preferably (0.2-1):1.

[0045] According to a preferred embodiment of the present invention, the mass concentration of the concentrated sulfuric acid is 80-98%, and the volume ratio of the concentrated sulfuric acid to the gel filtrate is (0.1-2):1, preferably (0.2-1):1 .

[0046] According to the present invention, in step (3), add water to dissolve the crude aluminum sulfate obtained in step (2), and filter to obtain calcium sulfate and decalcification filtrate. Too little water may lead to incomplete dissolution of aluminum sulfate crystals and excessive loss. Adding too much water will dissolve a small amount of calcium sulfate and reduce the efficiency of impurity remova...

Embodiment 1

[0069] Take 100g of coal sample A, mix it with 80g of sodium hydroxide and 320ml of water, and then stir and react in an autoclave at 230°C for 3 hours. After filtering and washing, add 10wt% dilute sulfuric acid to the filter cake according to the acid to dry filter cake weight ratio of 1.4:1, leach at 75°C for 30 minutes, filter and wash to obtain acidic waste liquid with a silicon dioxide content of 1.5%. Gel at 60°C for 6 hours, filter to obtain silica gel and gel filtrate. According to the volume ratio of concentrated sulfuric acid (90wt%) and gel filtrate of 0.6, concentrated sulfuric acid is added to the gel filtrate to obtain crude aluminum sulfate precipitate after a salting out. According to the volume mass ratio of water and crude aluminum sulfate being 1.0, water is added to dissolve the crude aluminum sulfate, and the calcium-removing filtrate is obtained after filtering. The purity of filter cake calcium sulfate is 98.3%. According to the volume ratio of concen...

Embodiment 2

[0071] Take 100g of coal gangue A, mix with 150g of sodium hydroxide and 100ml of water, knead and react at 150°C for 9 hours after mixing. Add water to dilute and cool down, filter and wash after 1 hour. According to the acid to dry filter cake ratio of 1.5:1, add 10wt% dilute hydrochloric acid to the filter cake, leach at 60°C for 30 minutes, and filter to obtain an acidic waste liquid with a silicon dioxide content of 10%. Gel at 20°C for 36 hours, filter to obtain silica gel and gel filtrate. According to the volume ratio of concentrated sulfuric acid (90wt%) and gel filtrate of 0.3, concentrated sulfuric acid is added to the gel filtrate to obtain crude aluminum sulfate. According to the volume mass ratio of water and crude aluminum sulfate of 2.0, water is added to dissolve the crude aluminum sulfate, and the calcium-removing filtrate is obtained after filtering. The purity of filter cake calcium sulfate is 98.2%. According to the volume ratio of concentrated sulfuric...

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PUM

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Abstract

The invention provides a method for preparing aluminum sulfate from an aluminum-containing acid treatment solution. The method comprises the following steps: (1) gelatinizing the aluminum-containing acid treatment solution, and filtering and separating to obtain gel and a gel filtrate; (2) adding concentrated sulfuric acid into the gel filtrate, and carrying out primary salting-out crystallization to obtain crude aluminum sulfate; (3) adding water to dissolve the crude aluminum sulfate, and filtering to obtain calcium sulfate and calcium-removed filtrate; (4) adding concentrated sulfuric acid into the calcium-removed filtrate, and carrying out secondary salting-out crystallization to obtain high-purity aluminum sulfate; and (5) evaporating and concentrating the secondary salting-out crystallization filtrate to obtain high-purity sodium sulfate precipitate. The invention develops the comprehensive treatment and resource utilization method aiming at the acid treatment waste liquid of minerals, especially the acid treatment waste liquid of a coal acid-base ash removal method. By adopting the method, aluminum oxide can be effectively extracted, aluminum sulfate can be prepared, and market requirements are met. And the method has very good industrial application value.

Description

technical field [0001] The invention relates to a method for preparing aluminum sulfate from an aluminum-containing acid treatment solution. Background technique [0002] The energy structure with relatively abundant coal and relatively poor oil and natural gas determines that China's energy consumption is dominated by coal. Electric coal and coking coal are the main uses of coal, and other uses include coal for chemical industry and building materials. Although the proportion of coal in primary energy consumption has shown a downward trend in recent years, the total consumption in 2015 was still 3.965 billion tons, accounting for more than 62.3%. In the next few decades, the current status of coal as the main energy consumption of the country will not change fundamentally. [0003] The types of coal in China are complex, the quality of the coal is generally poor, and the ash content is relatively high. After years of mining, the quality of the coal has continued to declin...

Claims

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Application Information

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IPC IPC(8): C01F7/74C01D5/16C01F11/46
CPCC01F7/743C01F7/748C01D5/16C01F11/46C01P2006/80
Inventor 赵利军李文华郭屹陈爱国靳凡
Owner CHNA ENERGY INVESTMENT CORP LTD
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