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Method for extracting aluminum oxide from fly ash

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

Inactive Publication Date: 2010-08-25
CHINA SHENHUA ENERGY CO LTD +1
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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 aluminum oxide from fly ash
  • Method for extracting aluminum oxide 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 aluminum oxide from fly ash. The method comprises the following steps of: a, acid-method treatment: mixing hydrochloric acid and fly ash, and transferring the mixture in a digester, of which the lining is made of polytetrafluoroethylene materials, for digestion, performing the separation of the pulp digested in a settling tank, evaporating and crystallizing upper-part overflow, baking the crystals to decompose the crystals into active coarse aluminum oxide and hydrogen chloride gas, wherein the hydrogen chloride gas is recovered to make acid and the acid is returned to the fly ash settling step; and b, bayer method treatment: mixing the active coarse aluminum oxide and circulating mother liquor, transferring the mixture in the digester for digestion, separating the pulp digested by settlement, performing refined filtration of the upper-part overflow to obtain refined solution, mixing the refined solution and aluminum hydroxide crystal seeds, decomposing the crystal seeds to obtain decomposed mother liquor and aluminum hydroxide, and filtering, washing and baking the aluminum hydroxide to obtain the aluminum oxide product, wherein the decomposed mother liquor is evaporated and then returned to the step of digesting the active coarse aluminum oxide. By adopting the method of the invention, the metallurgical-grade aluminum oxide meeting the requirements on national standards 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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IPC IPC(8): C01F7/02B09B3/00
Inventor 陈德郭昭华张万德池君洲陈可华张文广
Owner CHINA SHENHUA ENERGY CO LTD
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