Method For Co-Extraction Of Vanadium, Titanium And Chromium From Vanadium Slag
US-2022356543-A1 · Nov 10, 2022 · US
US11478672B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11478672-B2 |
| Application number | US-202016809685-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 5, 2020 |
| Priority date | Mar 6, 2019 |
| Publication date | Oct 25, 2022 |
| Grant date | Oct 25, 2022 |
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The present invention discloses a method for detoxifying chromium slag by using high sulfur coal. The method includes: sieving chromium slag into coarse-grained chromium slag and fine-grained chromium slag, air-drying and crushing both the coarse-grained chromium slag and the fine-grained chromium slag; separately mixing the crushed coarse-grained chromium slag and fine-grained chromium slag with the crushed high sulfur coal uniformly; adjusting pH values of a coarse-grained slag mixture and a fine-grained slag mixture to 8.0-11.0 and moisture content thereof to 12%-18%; conducting reduction on the treated coarse-grained slag mixture and fine-grained slag mixture, where the reduction temperature of the fine-grained slag mixture is 500-700° C., the reduction time of the fine-grained slag mixture is 10-30 min, the reduction temperature of the coarse-grained slag mixture is 800-1000° C., the reduction time of the coarse-grained slag mixture is 10-30 min; after the reduction, conducting water quenching, and discharging the product.
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What is claimed is: 1. A method for detoxifying chromium slag by using high sulfur coal, specifically comprising the following steps: (1) sieving chromium slag into coarse-grained chromium slag and fine-grained chromium slag, wherein a grain size of the coarse-grained chromium slag is greater than or equal to 10 meshes, and a grain size of the fine-grained chromium slag is less than 10 meshes; air-drying and crushing both the coarse-grained chromium slag and the fine-grained chromium slag; and air-drying and crushing high sulfur coal; (2) separately mixing the crushed coarse-grained chromium slag and fine-grained chromium slag in step (1) with the high sulfur coal uniformly, to obtain a coarse-grained slag mixture and a fine-grained slag mixture; (3) adjusting pH values of the coarse-grained slag mixture and the fine-grained slag mixture in step (2) to 8.0-11.0 and moisture content thereof to 12%-18% by spraying water or an acid solution; (4) separately conducting stirring and reduction on the treated coarse-grained slag mixture and fine-grained slag mixture in step (3) in a rotary kiln, wherein the reduction temperature of the fine-grained slag mixture is 500-700° C., the reduction time of the fine-grained slag mixture is 10-30 min, the reduction temperature of the coarse-grained slag mixture is 800-1000° C., and the reduction time of the coarse-grained slag mixture is 10-30 min; and (5) mixing reduced coarse-grained slag mixture and fine-grained slag mixture in step (4), conducting water quenching for cooling the slag mixture to below 300° C., and discharging the product. 2. The method for detoxifying chromium slag by using high sulfur coal according to claim 1 , wherein the coarse-grained chromium slag, the fine-grained chromium slag, and the high sulfur coal in step (1) are air-dried at normal temperature for more than 24 h, and the coarse-grained chromium slag, the fine-grained chromium slag, and the high sulfur coal are all crushed until they can pass through a sieve of 20 meshes. 3. The method for detoxifying chromium slag by using high sulfur coal according to claim 1 , wherein in step (2), the mass fractions of chromium slag in the coarse-grained slag mixture and the fine-grained slag mixture are 85%-95%, and the mass fraction of high sulfur coal is 5%-15%. 4. The method for detoxifying chromium slag by using high sulfur coal according to claim 1 , wherein the acid solution in step (3) is a dilute H 2 SO 4 solution or a FeSO 4 solution. 5. The method for detoxifying chromium slag by using high sulfur coal according to claim 1 , wherein the rotary kiln in step (4) is internally provided with a helical stirring device; the helical stirring device comprises a helical blade ( 1 ) and a rotary rod ( 2 ); the rotary rod ( 2 ) traverses the rotary kiln; and the helical blade ( 1 ) is arranged on the rotary rod ( 2 ). 6. The method for detoxifying chromium slag by using high sulfur coal according to claim 1 , wherein a solvent for the water quenching in step (5) is water or a FeSO 4 solution, and the mass fraction of the FeSO 4 solution is 1%-5%.
by reduction, e.g. hydrogenation · CPC title
Obtaining chromium · CPC title
Inorganic substances · CPC title
containing heavy metals · CPC title
Combined processes involving two or more distinct steps covered by groups A62D3/10 - A62D3/40 · CPC title
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