Method for extracting and enriching rare and precious metals from spent catalyst
A technology for ineffective catalysts and rare precious metals, applied in chemical instruments and methods, self-melt pulling method, improvement of process efficiency, etc., can solve the problems of increasing the recovery effect, not explaining the recovery effect, affecting the recovery rate of precious metals, etc. Low melting temperature and the effect of improving purity
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Embodiment 1
[0029] Such as figure 1 As shown, the method for extracting and enriching rare and precious metals from spent catalysts comprises the following steps:
[0030] Step 1, the spent catalyst to be treated (automobile exhaust gas purification catalyst, ZrO 2 , CeO 2 , La 2 o 3 、Nd 2 o 3 The contents are 5.9wt%, 4.5wt%, 0.58wt% and 0.46wt% respectively; the contents of platinum, palladium and rhodium are 522 g / t, 546 g / t and 143 g / t respectively), reducing agent (coke) and Copper oxide (Cu 2 O, the amount of copper oxide added is 1 / 8 of the mass of the spent catalyst, Cu2 The mass ratio of O to the reducing agent is 8:1) First, perform low-temperature reduction at 200°C for 25 minutes, and then add silicon material after low-temperature reduction (the silicon material is metallurgical grade silicon, with a purity of 98.6%, and the amount of silicon material added is pending failure. 60% of the mass of the catalyst) and additives (the additives are CaO and SiO with a mass rat...
Embodiment 2
[0035] Such as figure 1 As shown, the method for extracting and enriching rare and precious metals from spent catalysts comprises the following steps:
[0036] Step 1, the spent catalyst to be treated (automobile exhaust gas purification catalyst, ZrO 2 , CeO 2 , La 2 o 3 、Nd 2 o 3 content of 5.9wt%, 4.5wt%, 0.58wt% and 0.46wt% respectively; content of platinum, palladium and rhodium are 522g / ton, 546g / ton and 143g / ton respectively), reducing agent (CO gas, CO gas flow rate is 200mL / min) and iron oxide (Fe 2 o 3 , the amount of iron oxide added is 1 / 9 of the mass of the spent catalyst) First, perform low-temperature reduction at 900°C for 2 hours, and then add silicon material after low-temperature reduction (silicon material is ferrosilicon alloy, the iron content in ferrosilicon alloy is 2wt%, silicon material The amount added is 75% of the mass of the spent catalyst to be treated) and additives (the additives are CaO and SiO with a mass ratio of 2:1 2 The mixture,...
Embodiment 3
[0041] Such as figure 1 As shown, the method for extracting and enriching rare and precious metals from spent catalysts comprises the following steps:
[0042] Step 1. The spent catalyst to be treated (carrier catalyst for the petrochemical industry, alumina as the carrier, containing 0.35wt% platinum), reducing agent (charcoal) and iron oxide (FeO, the amount of iron oxide added is 2% of the mass of the spent catalyst 1 / 5, the mass ratio of charcoal to FeO is 1:4) first perform low-temperature reduction at 1000°C for 3 hours, and then add silicon material after low-temperature reduction (the silicon material is elemental silicon, with a purity of 98.6wt%, and the amount of silicon material added The ratio to the mass of the spent catalyst to be treated is 1:1) and additives (the additives are CaO, SiO with a mass ratio of 4:1:0.5 2 and MgO mixture, the amount of additive added is 65% of the mass of the spent catalyst to be treated) at a temperature of 1650 ° C for high-temp...
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