Method for wet-process extraction of alumina from high-aluminum fly ash

A high-alumina fly ash and alumina technology, which is applied to the removal of alumina/hydroxide and solid waste, can solve the problems of harsh reaction conditions, acid process equipment corrosion, and difficult operation, and achieve low equipment material requirements , Reduce production energy consumption and avoid a large number of cycles

Active Publication Date: 2016-11-23
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

Among them, the acid method has disadvantages such as serious corrosion of equipment, difficulty in acid medium recovery, and unreachable product quality; the sintering method has disadvantages such as high sintering temperature, high energy consumption, and large amount of tailings; Disadvantages such as large and large ammonia emissions
Recently, Chinese patent application CN103663516A discloses a method for preparing aluminum hydroxide by using high-alumina fly ash. The process features mainly include two-step desiliconization and two-step high-temperature dissolution reaction. This process can realize the formation of aluminum and silicon in fly ash. However, the process is complicated and the operation is difficult. Two-step desiliconization pretreatment is adopted, and pickling activation is also used. It is difficult to recycle the pickling solution, which is easy to cause environmental pollution. The two-step dissolution reaction conditi

Method used

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  • Method for wet-process extraction of alumina from high-aluminum fly ash
  • Method for wet-process extraction of alumina from high-aluminum fly ash

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] The raw material is high-alumina fly ash from a place in Inner Mongolia as an example, and its main chemical composition is shown in Table 1:

[0031] Table 1 Chemical composition of high alumina fly ash

[0032]

[0033] Such as figure 1 Shown, a kind of method of wet extraction alumina from high aluminum fly ash, described method may further comprise the steps:

[0034] 1. the high-alumina fly ash described in Table 1 is mixed with 13.5% sodium hydroxide solution by volume to mass ratio of 5:1 (ml / g) with the mass fraction, and the pre-desilication reaction is carried out in the reactor. The temperature is 100°C, and the reaction time is 2 hours. After the reaction, the pre-desiliconized fly ash and the desiliconized liquid are obtained by filtration and separation; after the pre-desiliconized fly ash is washed and dried, the A / S is measured to be 2.4.

[0035] 2. Combine the dried pre-desiliconized fly ash with sodium oxide concentration of 600g / L, Na2 O and Al ...

Embodiment 2

[0041] Such as figure 1 Shown, a kind of method of wet extraction alumina from high aluminum fly ash, described method may further comprise the steps:

[0042] 1. the high-alumina fly ash described in Table 1 and the mass fraction are 20% sodium hydroxide solution by volume and mass ratio is 3: 1 (ml / g) mix, carry out pre-desilication reaction in reactor, reaction temperature The temperature is 120°C, and the reaction time is 0.5h. After the reaction is completed, the pre-desiliconized fly ash and the desiliconized liquid are obtained by filtration and separation; after the pre-desiliconized fly ash is washed and dried, the measured A / S is 2.4.

[0043] 2. The dried pre-desiliconized fly ash and sodium oxide concentration 400g / L, Na 2 O and Al 2 o 3 The sodium aluminate solution with a molar ratio of 20 or 10 is mixed according to the volume to mass ratio of 3:1 (ml / g), placed in a reaction kettle, and kept at 110°C for 1d for low-temperature wet dissolution reaction, and f...

Embodiment 3

[0049] 1. the high-alumina fly ash described in Table 1 is mixed with 10% sodium hydroxide solution by volume to mass ratio as 6:1 (ml / g) with the mass fraction, and the pre-desilication reaction is carried out in the reactor, and the reaction temperature The temperature is 80°C, and the reaction time is 2 hours. After the reaction is completed, it is filtered and separated to obtain the pre-desiliconized fly ash and desiliconized liquid; after the pre-desiliconized fly ash is washed and dried, the measured A / S is 2.4

[0050] 2. The dried pre-desiliconized fly ash and sodium oxide concentration 500g / L, Na 2 O and Al 2 o 3 The sodium aluminate solution with a molar ratio of 30 or 13 is mixed according to the volume to mass ratio of 4:1 (ml / g), placed in a reaction kettle, and kept at 140°C for 0.5d for low-temperature wet dissolution reaction. Filtration and separation to obtain low-temperature dissolution slag and low-temperature dissolution liquid, the concentration of sil...

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Abstract

The invention provides a method for wet-process extraction of alumina from high-aluminum fly ash, and the method comprises the following steps: 1)silicon pre-removal treatment of the high-aluminum fly ash; 2)low temperature wet dissolution of part of alumina from silicon-pre-removed fly ash; 3)high temperature wet dissolution of the alumina from low temperature dissolution slag; 4)mixing of dissolution solutions of the step 2)and the step 3)and seeded precipitation spent liquor for evaporation concentration crystallization for preparation of hydrated sodium aluminate crystals, or mixing of the dissolution solution of the step 2)and the seeded precipitation spent liquor for evaporation concentration crystallization for preparation of the hydrated sodium aluminate crystals, and returning of the dissolution solution of the step 3)back to the step 2)as a dissolution medium; and 5)dissolving of the hydrated sodium aluminate crystals in a dilute alkali solution, silicon removal and seed decomposition to obtain aluminum hydroxide, and calcination to obtain an alumina product. According to the method, the alumina is step-by-step dissolved, dissolution temperature and dissolution pressure are low, energy consumption is low, requirement of equipment materials is low, process is simple, aluminum and silicon both are effectively utilized, and the method adopts a full-wet process, and is suitable for industrial production.

Description

technical field [0001] The invention relates to the utilization of high-aluminum fly ash, in particular to a method for wet extraction of alumina from high-alumina fly ash. Background technique [0002] my country's alumina output accounts for 1 / 3 of the world, but my country's bauxite resource reserves account for only 3% of the world's total, the resource guarantee period is less than 10 years, and the alumina's external dependence exceeds 50%. Due to the tight mineral export policy, the contradiction between the supply of bauxite resources in my country has become increasingly prominent. [0003] In my country, Inner Mongolia, Shanxi and other places are rich in high-aluminum coal resources, and the amount of resources buried at a depth of more than 500 meters is nearly 50 billion tons. The content of aluminum is 35% to 50%, which is equivalent to the content of alumina in low-grade bauxite in my country. At present, the total amount of high-aluminum fly ash has exceeded ...

Claims

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Application Information

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IPC IPC(8): C01F7/02B09B3/00
Inventor 马淑花汪泽华张宏王晓辉郑诗礼张懿唐振华
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI
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