A method for extracting and removing iron from aluminum chloride slurry
A technology of aluminum chloride and purification method, applied in the directions of aluminum chloride, aluminum halide, etc., can solve the problems of less use of extractant and consumption of extractant, and achieve the effect of reducing use and volume
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Embodiment 1
[0029] Take iron-containing aluminum chloride slurry with a solid content of 30wt%, adjust the pH value of the slurry to 1 with 4wt% hydrochloric acid solution, and set aside.
[0030] Prepare the extracted organic phase and set aside. The formula of the extracted organic phase is: 30vol% trioctyl tertiary amine and 70vol% sulfonated kerosene. Among them, trioctyl tertiary amine (N235, produced by Luoyang Aoda Chemical Co., Ltd.) was used as the extractant, and sulfonated kerosene (produced by Baorun Chemical Co., Ltd.) was used as the diluent.
[0031] The above-mentioned extracted organic phase and slurry were mixed in the extraction tank according to the volume shown in Table 1, the extraction temperature was controlled at 20° C., stirred in the extraction tank for 0.1 hour, and allowed to stand for 0.1 hour. After the organic phase and the aqueous phase are divided into upper and lower layers, the upper organic phase is extracted through the overflow device provided in th...
Embodiment 2
[0036] The iron-containing aluminum chloride slurry with a solid content of 40 wt % was taken, and the pH value of the slurry was adjusted to 2 with 4 wt % hydrochloric acid solution.
[0037] Prepare the extracted organic phase and set aside. The formula for extracting the organic phase is: 40vol% bis(2-ethylhexyl phosphoric acid) and 60vol% sulfonated kerosene. Among them, bis(2-ethylhexyl phosphoric acid) (P204, produced by Jiangxi Shanggao County Yongsheng Chemical Co., Ltd.) was used as the extractant, and sulfonated kerosene (produced by Baorun Chemical Co., Ltd.) was used as the diluent.
[0038]The above-mentioned extracted organic phase and slurry were mixed in the extraction tank according to the volume described in Table 1, the extraction temperature was controlled at 30° C., stirred for 1 hour in the extraction tank, and left to stand for 0.1 hour. After the organic phase and the aqueous phase are divided into upper and lower layers, the upper organic phase is ext...
Embodiment 3
[0043] The iron-containing aluminum chloride slurry with a solid content of 50 wt % was taken, and the pH value of the slurry was adjusted to 3 with 4 wt % hydrochloric acid solution.
[0044] Prepare the extracted organic phase and set aside. The formula of the extracted organic phase is: 50vol% tributyl phosphate and 50vol% sulfonated kerosene. Among them, tributyl phosphate (TBP, produced by Jiangxi Shanggao County Yongsheng Chemical Co., Ltd.) was used as the extractant, and sulfonated kerosene (produced by Baorun Chemical Co., Ltd.) was used as the diluent.
[0045] The above-mentioned extracted organic phase and slurry were mixed in the extraction tank according to the volume shown in Table 1, the extraction temperature was controlled at 40° C., stirred in the extraction tank for 1.5 hours, and allowed to stand for 0.1 hour. After the organic phase and the aqueous phase are divided into upper and lower layers, the upper organic phase is extracted through the overflow de...
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