Method for extracting alumina from fly ash

A technology of fly ash and alumina, which is applied to the removal of alumina/hydroxide and solid waste, etc. It can solve the problem that it cannot be used industrially, can only be used for laboratory research, increases the production cost of alumina, and affects the surrounding environment to improve the dissolution effect, facilitate the sedimentation of slag, and prolong the service life

Active Publication Date: 2011-08-10
CHINA SHENHUA ENERGY CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantage is that it is difficult to remove iron and impurities, the quality of alumina products is different from the traditional national standards, and some technological problems still need to be studied and tested
[0008] Patent application CN 1927716A discloses a method for extracting alumina in fly ash, which has the advantage of combining the advantages of acid and alkali methods for preparing alumina, but due to the limitation of process equipment, this method has the following problems: using The "negative pressure concentration in the concentration tank" process is economically unreasonable, so the evaporation process cannot be used industrially, and can only be used for laboratory research; the dissolved slurry is separated and washed in the settling tank to obtain the liquid content of the leaching residue As high as 70-80wt%, it is directly sent to the waste residue dump, which has a great impact on the surrounding environment; the acid dissolution temperature is 90-110°C, and it is found through experiments that the hydrochloric acid dissolution rate of alumina at this temperature is only about 60%, and the dissolution rate is too low It increases the production cost of alumina
Therefore, it is necessary to develop a reliable process method to improve the dissolution effect of alumina in fly ash and solve the problem of corrosion of equipment by hydrochloric acid medium at high temperature

Method used

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  • Method for extracting alumina from fly ash
  • Method for extracting alumina from fly ash

Examples

Experimental program
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Effect test

Embodiment 1

[0041] By 85% Al 2 o 3 Dissolution rate calculates the consumption of hydrochloric acid, the high aluminum fly ash (Al 2 o 3 Content 48.2wt%, SiO 2 content of 38.33wt%) and hydrochloric acid with a concentration of 28wt% to make fly ash slurry, sent to the dissolution device lined with polytetrafluoroethylene material, stayed at 150 ° C for 1.5 hours and kept stirring, and the dissolved material Slurry is sent to the settling tank for primary separation, the underflow acid slag from the settling tank enters the washing tank, and reverse washing is carried out 5 times with hot water at 85°C. The dissolved slurry can be diluted, the acid slag after the last washing is filtered through the filter, the filtrate is returned to the washing tank, the water content of the filter cake is controlled to be ≤35wt%, the filter cake is sent to the waste residue yard, and the overflow of the settling tank is sent to Go to the 3-effect forced circulation evaporator, and get AlCl after eva...

Embodiment 2

[0044] By 80% Al 2 o 3 Dissolution rate calculates the consumption of hydrochloric acid, the high aluminum fly ash (Al 2 o 3 Content 42.5wt%, SiO 2 Content 40.38wt%) and concentration are 25wt% hydrochloric acid batching to make fly ash slurry, send to the stripper identical with embodiment 1, stay 2.0 hours under 142 ℃ of conditions and constantly stir, the slurry of stripping Send it to the settling tank for a separation, send the underflow acid slag from the settling tank to the washing tank, and perform 6 reverse washings with 80°C hot water. The amount of hot water added is 2.5t / t of acid slag. The liquid can dilute the dissolved slurry, the acid residue after the last washing is filtered through the filter, the filtrate is returned to the washing tank, the moisture content of the filter cake is controlled to be ≤35wt%, the obtained filter cake is sent to the waste residue yard, and the overflow of the settling tank is sent to Go to the 4-effect forced circulation eva...

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Abstract

The invention discloses a method for extracting alumina from fly ash. The method comprises the following steps of: a), acid treatment, i.e. mixing and feeding hydrochloric acid and the fly ash into a digester lined with a polyfluortetraethylene material for dissolving, carrying out separation on dissolved slurry by a settling tank, carrying out evaporation, crystallization, roasting and decomposition on the upper overflow slurry to form active initial alumina and hydrogen chloride gas, and returning the hydrogen chloride gas to a fly ash dissolving process after the hydrogen chloride gas is recovered to prepare acid; and b), Bayer process treatment, i.e. mixing the active initial alumina and circulating mother liquor, sending the mixture into an autoclave for dissolving, carrying out separation on the dissolved slurry by the settling tank, carrying out fine filtering on the upper overflow slurry to obtain refined fluid, mixing the refined fluid and seed crystals of aluminium hydroxide, carrying out seed crystal digestion to obtain decomposition mother liquor and aluminium hydroxide, returning the decomposition mother liquor to the process of dissolving the active initial alumina after the decomposition mother liquor is evaporated, and carrying out filtering, washing and roasting on the aluminium hydroxide to obtain an alumina product. Due to the adoption of the method, the metallurgical alumina which meets the national standard requirements can be prepared.

Description

technical field [0001] The invention relates to a method for extracting alumina from fly ash, more specifically, to a method for extracting metallurgical grade alumina by treating high-alumina fly ash with hydrochloric acid-Bayer method. Background technique [0002] At present, about 70 million tons of alumina are produced every year in the world, and almost all alumina plants use bauxite as raw material. my country is the world's largest producer of alumina, producing about 21 million tons of alumina in 2008, accounting for about 30% of the world's total output. However, my country's bauxite resources are relatively poor, and the bauxite reserves only account for about 6% of the world's total reserves. The ore grade is low, and the ore type is mainly difficult to handle. , and the production cost is also higher. Due to the shortage of bauxite resources in my country, my country imported about 25 million tons of bauxite ore in 2008, accounting for about 50% of the domestic...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01F7/02B09B3/00
Inventor 陈德凌文郭昭华张万德池君洲陈可华张建民张文广
Owner CHINA SHENHUA ENERGY CO LTD
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