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Применить Всего найдено 2. Отображено 2.
26-03-2014 дата публикации

Method for preparing aluminum hydroxide by utilizing high-alumina coal ash

Номер: CN103663516A
Принадлежит:

The invention relates to a method for preparing aluminum hydroxide by utilizing high-alumina coal ash. By adopting the deep desilicication process and the two-step sub-molten salt dissolution process, not only can the secondary enrichment of the silicon component be realized, but also the aluminum component can be adequately dissolved under the low temperature and low pressure, the operation condition is moderate, the silicon and aluminum can be adequately utilized, and the dissolution rate of the aluminum can reach more than 95 percent. The method comprises the following steps: pretreating the high-alumina coal ash in a deep desilicication way; primarily dissolving; secondarily dissolving; concentrating and crystallizing the dissolution liquid; dissolving hydrated sodium aluminate crystals; performing desilicication on the sodium aluminate coarse liquid; seed precipitating the aluminium hydroxide; and dealkalizing tailings. The obtained desilicication liquid can be used for preparing a ...

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26-08-2015 дата публикации

Method for extracting alumina from fly ash through sulfo ammonium salt mixing medium system

Номер: CN104860338A
Принадлежит:

The invention relates to a method for extracting alumina from fly ash through a sulfo ammonium salt mixing medium system. The method comprises: adopting solid waste fly ash discharged from coal-fired power plant or boiler as a raw material, and carrying out strengthening leaching in a sulfo ammonium salt mixing medium system at a high temperature of 120-240 DEG C, wherein the leaching time is 0.5-6 h; maintaining the system at a temperature of 75-95 DEG C after the leaching, and filtering to obtain the primary filtrate and the primary filtration residue; cooling the primary filtrate to a temperature of 10-30 DEG C by using the characteristic of the large change of the ammonium aluminum sulfate solubility along with the temperature change so as to precipitate the ammonium aluminum sulfate solid; washing the primary filtration residue at a temperature of 85-95 DEG C, and filtering to obtain the secondary filtrate and the secondary filtration residue; carrying out evaporation concentration ...

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