Method for using aluminum ash to prepare aluminum polychlorid and co-produce calcium fluoride

A technology of polyaluminum chloride and co-production of calcium fluoride, which is applied in the fields of aluminum chloride, chemical instruments and methods, aluminum halide, etc., and can solve problems such as air pollution, no systematic process, and no consideration of the direction of fluoride

Inactive Publication Date: 2019-07-23
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

Because the primary aluminum ash contains more than 40% elemental aluminum, the elemental aluminum in it can be recovered after frying ash. The secondary aluminum ash with a smaller particle size cannot be recycled due to the low content of elemental aluminum.
Secondary aluminum ash contains aluminum nitride and fluoride, and direct discharge will cause serious water, soil, and air pollution
Although the method disclosed above realizes the deep hydrolysis of aluminum nitride, it does not consider the direction of fluoride, resulting in the purified aluminum ash is still a hazardous waste, and neither of them has formed a systematic process, only for certain characteristics of aluminum ash Components are utilized as resources, resulting in secondary waste residue / waste water, and continuous operation has not yet been realized

Method used

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  • Method for using aluminum ash to prepare aluminum polychlorid and co-produce calcium fluoride
  • Method for using aluminum ash to prepare aluminum polychlorid and co-produce calcium fluoride

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Experimental program
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Effect test

Embodiment 1

[0022] The aluminum ash is treated according to the process of catalytic hydrolysis-acidolysis, catalytic hydrolysis section: liquid-solid ratio 2ml / g, reaction temperature 70°C, reaction time 1h, hydrolyzate circulation times 3 times; acidolysis section: liquid-solid ratio 3ml / g g, reaction temperature 80°C, reaction time 1h, hydrochloric acid concentration 100g / l. Industrial calcium fluoride and polyaluminum chloride were prepared, the content of polyaluminum chloride was 6.2% alumina, the basicity was 80%, the content of ammonia nitrogen was 0.02%, and the content of fluorine was 0.03%.

Embodiment 2

[0024] The aluminum ash is treated according to the process of catalytic hydrolysis-acidolysis, catalytic hydrolysis section: liquid-solid ratio 3ml / g, reaction temperature 85°C, reaction time 2h, hydrolyzate cycle times 5 times; acidolysis section: liquid-solid ratio 4ml / g g, reaction temperature 80°C, reaction time 1h, hydrochloric acid concentration 150g / l. Industrial calcium fluoride and polyaluminum chloride are prepared, the content of polyaluminum chloride is 6% alumina, the basicity is 70%, the content of ammonia nitrogen is 0.01%, and the content of fluorine is 0.02%.

Embodiment 3

[0026] The aluminum ash is treated according to the process of catalytic hydrolysis-acidolysis, catalytic hydrolysis section: liquid-solid ratio 3ml / g, reaction temperature 95°C, reaction time 3h, hydrolyzate cycle times 6 times; acidolysis section: liquid-solid ratio 5ml / g g, reaction temperature 95°C, reaction time 2h, hydrochloric acid concentration 200g / l. Industrial calcium fluoride and polyaluminum chloride are prepared, the content of polyaluminum chloride is 10% alumina, the basicity is 65%, the content of ammonia nitrogen is 0.009%, and the content of fluorine is 0.001%.

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Abstract

The invention discloses a method for using aluminum ash to prepare aluminum polychlorid and co-produce calcium fluoride. The method comprises the steps that filtrate and a filter cake are obtained through catalytic hydrolysis, filtration and washing of aluminum ash, and a fluorine rich solution is obtained through multiple recycling of the filtrate; an aluminum rich solution, washing liquid and acidolysis residue are obtained through acidolysis, filtration and washing of the filter cake; calcium fluoride and denitration ammonium hydroxide are prepared through precipitation and filtration of the fluorine rich solution; an aluminum polychlorid water purifying agent is prepared through polymerization mediation of the aluminum rich solution obtained through acidolysis, and a fireproof materialis prepared through drying and sintering of acidolysis residue. The method disclosed by the invention achieves thorough hydrolysis of aluminum nitride and directional enrichment and separation of impurity ions, the ammonia-nitrogen content of the aluminum polychlorid is low, the quality is high, the performance indexes are completely superior to the requirement of GB / T22627-2014 standard, the calcium fluoride purity is high, and the aluminum polychlorid can replace industrial calcium floride. The method solves the problem of safe treatment of aluminum ash, and achieves resource utilization, and the environmental, economical and social benefits are outstanding.

Description

technical field [0001] The invention relates to the field of hazardous waste safe disposal, resource utilization and sewage treatment, in particular to a new method for preparing polyaluminum chloride and co-producing calcium fluoride by using aluminum ash. Background technique [0002] Aluminum ash is a hazardous waste produced by aluminum electrolysis, aluminum processing and aluminum recycling industries, with an annual emission of more than 4 million tons. The electrolytic aluminum industry produces about 10-50kg of aluminum ash for every 1 ton of aluminum produced. Because the primary aluminum ash contains more than 40% elemental aluminum, the elemental aluminum in it can be recovered through frying ash treatment, and the secondary aluminum ash with a smaller particle size cannot be recycled due to the low content of elemental aluminum. Secondary aluminum ash contains aluminum nitride and fluoride, and direct discharge will cause serious water, soil, and air pollution. ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01F7/56C01F11/22C02F1/52
CPCC01F7/56C01F11/22C02F1/5236
Inventor 李占兵李少鹏李会泉孙振华张建波
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI
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