Comprehensive recovery method for multi-metal from dead catalyst
A waste catalyst and multi-metal technology, which is applied in the field of catalyst secondary resource recovery, can solve the problems of discarded renewable resources, difficulty in recycling, low resource recovery rate, etc., and achieve the effects of energy saving, process and cost saving, and wide adaptability
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[0041] Example 1:
[0042] Take 1000g of high nickel catalyst from a petrochemical plant, and use sulfuric acid with a liquid-solid ratio of 5:1 and 100g / L in the stirred mill. The prepreg residue is matured by adding concentrated sulfuric acid. The acid mass ratio of the residue is 4:1. The temperature is 106℃, and the curing time is 48h. The matured residue is leached with a prepreg, the leaching temperature is 80℃, and the leaching time is 4h. After pre-soaking and aging water leaching, the leaching rate of vanadium was 88.0%, and that of aluminum was 9.3%. The obtained leaching slag is mixed with silica and reduced iron powder and smelted at 1350°C for 2 hours to obtain the matte phase and the slag item. The matte incorporation rates of nickel, cobalt, and molybdenum are 90%, 89%, and 82%, respectively. The matte phase obtains nickel, cobalt, and molybdenum products according to conventional metallurgical methods.
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[0043] Example 2:
[0044] Take 1000g of high-cobalt waste catalyst from a petrochemical company. The vanadium content in this catalyst is very low and has no recycling value. Therefore, it is directly pyro-smelted. According to the specific composition of the catalyst, 280g silica and 420g reduced iron powder are added. After smelting at 1350℃ for 2h, the matte phase and slag phase are obtained. The matte incorporation rates of nickel, cobalt and molybdenum are 94%, 95%, and 79% respectively. The matte phase obtains nickel, cobalt, and molybdenum products according to conventional metallurgical methods.
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