A method of recovering metal elements from spent catalysts
A technology for waste catalysts and metal elements, applied in the direction of improving process efficiency, can solve the problems of short process flow, complicated operation, long process flow, etc., and achieve the effect of short process flow, simple operation, clean cost and environmental protection
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0054] This example is used to illustrate the method of the present invention for recovering metal elements from spent catalysts.
[0055] (1) 1000g spent hydrogenation catalyst (the content of nickel element is 10.7% by weight, the content of cobalt element is 0.3% by weight, the content of tungsten element is 1.6% by weight, the content of molybdenum element is 0.9% by weight, the content of vanadium element 5.1% by weight, the content of carbon element is 27.4% by weight, the content of sulfur element is 8.6% by weight, the content of alumina is 25% by weight), 940g of ferrous laterite ore (the content of iron element is 45% by weight), 191g of Silicon, 316g of calcium oxide, 60g of coke powder (the content of carbon element is 86% by weight) and 100g of calcium fluoride were smelted by fire method at 1570°C for 2 hours, and the alloy was extracted. The recovery rate of nickel obtained in this step was 99.79%, and the recovery of cobalt The recovery rate of molybdenum is 99...
Embodiment 2
[0061] This example is used to illustrate the method of the present invention for recovering metal elements from spent catalysts.
[0062](1) 1000g spent hydrogenation catalyst (the content of nickel element is 3.44% by weight, the content of cobalt element is 1.48% by weight, the content of tungsten element is 0.73% by weight, the content of molybdenum element is 5.84% by weight, the content of vanadium element 0.54% by weight, the content of carbon element is 28% by weight, the content of sulfur element is 7% by weight, the content of alumina is 28% by weight), 1500g ferrous laterite ore (the content of iron element is 47% by weight), 306g of Silicon, 350g of calcium oxide, 160g of coke powder (the content of carbon element is 89% by weight) and 30g of sodium fluoride were smelted by fire method at 1650°C for 1.5h, and the alloy was extracted. This step obtained a nickel recovery of 99.4%, cobalt The recovery rate was 99.29%, the recovery rate of molybdenum was 99.78%, the r...
Embodiment 3
[0068] This example is used to illustrate the method of the present invention for recovering metal elements from spent catalysts.
[0069] (1) 1000g spent hydrogenation catalyst (the content of nickel element is 4.89% by weight, the content of cobalt element is 1.28% by weight, the content of tungsten element is 1.95% by weight, the content of molybdenum element is 3.95% by weight, the content of vanadium element 2.11% by weight, the content of carbon element is 28% by weight, the content of sulfur element is 9% by weight, the content of alumina is 39.8% by weight), 1180g irony laterite ore (the content of iron element is 45% by weight), 352g of Silicon, 398g calcium oxide, 100g coke powder (the content of carbon element is 85% by weight), 100g calcium fluoride were smelted by fire method at 1600°C for 3 hours, and the alloy was extracted. The recovery rate of nickel obtained in this step was 99%, and the recovery rate of cobalt was The recovery rate of molybdenum is 99%, the ...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More