Method for recycling alumina and sodium oxide from bayer process red mud
A Bayer process red mud and alumina technology, applied in the direction of alumina/aluminum hydroxide, alkali metal oxides, etc., can solve problems such as excessive requirements, difficulty in meeting high-efficiency circulation of media, and thermodynamic limitations
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Embodiment 1
[0066] With the method for recovering alumina and sodium oxide from Bayer process red mud of the present invention, the red mud of a certain Bayer process alumina plant in Henan is used as raw material to recover alumina and sodium oxide. The red mud composition of the alumina plant (mass percentage, wt%, the same below) as described in Table 1:
[0067] Table 1
[0068]
[0069] Its production process is as figure 1 The methods shown include:
[0070] (1) Mix the red mud of an alumina factory in Henan with concentrated sodium hydroxide solution to prepare a slurry with a liquid NaOH mass fraction of 40% and a ratio of liquid NaOH mass to dry red mud mass of 2.5:1. And add lime to make CaO and SiO in the solid phase 2 The ratio of the amount of the substance is 1.4:1, and then the slurry is placed in a high-pressure reactor for a stripping reaction. The stripping reaction temperature is 210 ° C, and the stripping time is 0.3 hours. The stripping solution containing sodiu...
Embodiment 2
[0076] With the method for reclaiming alumina and sodium oxide from Bayer process red mud of the present invention, the red mud of a certain Bayer process alumina plant in Henan as described in Table 1 is still used as raw material to reclaim alumina and sodium oxide, and the production process is as follows Said:
[0077] (1) Mix the crystallization mother liquor of Example 1 with the prepared concentrated NaOH solution and the Bayer process red mud evenly, and adjust the liquid phase NaOH mass fraction to 50%, and the ratio of the liquid phase NaOH mass to the dry basis red mud mass is 3:1 slurry, and add lime to make CaO and SiO in the solid phase 2 The ratio of the amount of the substance is 1.6:1, and then the slurry is placed in a high-pressure reactor for a stripping reaction. The stripping reaction temperature is 240 ° C, and the stripping time is 0.2 hours, and the stripping solution containing sodium aluminate and slag are obtained. The solid-liquid mixture, the rel...
Embodiment 3
[0083] With the method for reclaiming alumina and sodium oxide from Bayer process red mud of the present invention, the red mud of a certain Bayer process alumina plant in Henan as described in Table 1 is still used as raw material to reclaim alumina and sodium oxide, and the production process is as follows Said:
[0084] (1) Mix the red mud of an alumina plant in Henan with concentrated sodium hydroxide solution to prepare a slurry with a liquid NaOH mass fraction of 55% and a ratio of liquid NaOH mass to dry red mud mass of 4:1. And add lime to make CaO and SiO in the solid phase 2 The ratio of the amount of the substance is 1.3:1, and then the slurry is placed in a high-pressure reactor for a stripping reaction. The stripping reaction temperature is 270 ° C, and the stripping time is 0.5 hours, and the stripping solution containing sodium aluminate and slag are obtained. The solid-liquid mixture, the relative dissolution rate of alumina entering the solution is 88.4%;
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