Lime slaking process for alumina production
A technology of alumina and lime, applied in the direction of alumina/aluminum hydroxide, etc., can solve problems such as increased alumina consumption and alkali consumption, hindering the dissolution of diaspore, and slow decomposition of hydrated garnet, etc., to achieve Effects of increasing effective production capacity, reducing red mud output rate, and increasing saturation coefficient
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Embodiment 1
[0021] With 30℃, Al 2 o 3 : 55g / l, SiO 2 : The aluminum hydroxide lotion of 0.42g / l digests industrial lime, and the solid content of the milk of lime after deslagging is 322g / l, and the raw ore pulp is prepared by using this milk of lime and the pulp after grinding, and after 8 hours of pretreatment After desiliconization, under the conditions of dissolution temperature 260°C, time 60min, dissolution liquid Nk 210g / l, conventional high-pressure dissolution was carried out, and the obtained red mud A / S was 1.46, and N / S was 0.21.
Embodiment 2
[0023] With 52℃, Al 2 o 3 : 79g / l, SiO 2 : 0.46g / l aluminum hydroxide lotion to digest industrial lime, the solid content of the milk of lime after deslagging is 179g / l, use this milk of lime, the concentrate obtained through flotation, and circulating lye to prepare and dissolve the raw ore slurry , pre-desilication and stripping conditions are the same as in Example 1, and the obtained stripping red mud has an A / S of 1.48 and an N / S of 0.19.
Embodiment 3
[0025] With 92℃, Al 2 o 3 : 58g / l, SiO 2 : 0.45g / l primary red mud washing liquid to digest industrial lime, the solid content of the milk of lime after deslagging is 285g / l, use this milk of lime, the concentrate obtained through flotation, and circulating lye to prepare and dissolve the raw ore slurry , pre-desilication and stripping conditions are the same as in Example 1, stripped red mud A / S is 1.52, N / S is 0.07.
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