Prepn process of iron red with salfated roasted dreg of sulfur containing aurin ore
A technology of sulfuration roasting and gold concentrate, applied in the direction of iron oxide, iron oxide/iron hydroxide, fibrous filler, etc., can solve the problems of rising raw material prices, air pollution, and shortage of raw materials, and increase the utilization of tailings resources efficiency, reduce environmental pollution, and improve efficiency
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Embodiment 1
[0012] Add 60% sulfuric acid in a reactor with a stirrer, start the stirrer to stir, add the calcined slag at one time, the weight ratio of the calcined slag and the sulfuric acid solution is 2:1, and the weight ratio of the calcined slag and the co-solvent is 1:1, The composition of co-solvent is 1% sodium edetate, 30% CuO, 20% Fe 2 o 3 , 40% SiO 2 and 9% Al 2 o 3 , Reaction at 80°C for 6 hours, the leaching rate of iron is 100%, and the leaching rate of gold and silver is over 98%. Filtrate, neutralize the filtrate with ammonia water until the pH value is 1, add flocculant ferric chloride to remove the precipitate, separate the co-solvent, and then add ammonia water at 50°C until the iron ions are completely precipitated. After filtering, the filtrate is used to recover ammonia water and alkali, and the filter residue is washed, dried and calcined at 300°C. The calcined iron red is ground to the particle size required by the iron red pigment, that is, high-quality iron ...
Embodiment 2
[0014] Add 30% sulfuric acid in the reactor with stirrer, start the mixer to stir, add calcined slag at one time, the weight ratio of calcined slag and sulfuric acid solution is 10:1, the weight ratio of calcined slag and co-solvent is 50:1, The composition of co-solvent is 25% sodium edetate, 1% CuO, 30% Fe 2 o 3 , 60% SiO 2 The reaction temperature is 100° C., the reaction time is 1 hour, the leaching rate of iron is 100%, and the leaching rate of gold and silver is over 98%. The extract was filtered, the temperature of the system was lowered to room temperature, and then filtered. The filtrate was neutralized with alkali to a pH value of 1.3, flocculant alum was added to remove the precipitate, and the co-solvent was separated, and then ammonia water was added at 90°C until the iron ions were completely precipitated. After filtration, the filtrate is used to recover ammonia water and alkali, and the filter residue is washed, dried and calcined at 680°C. The calcined iro...
Embodiment 3
[0016] Add 45% sulfuric acid in the reactor with stirrer, start the mixer to stir, add calcined slag at one time, the weight ratio of calcined slag and sulfuric acid solution is 5: 1, the weight ratio of calcined slag and co-solvent is 100: 1, The composition of co-solvent is 10% sodium edetate, 2% CuO, 15% Fe 2 o 3 , 50% SiO 2 and 5% Al 2 o 3 The reaction temperature is 60°C, the reaction time is 5 hours, the leaching rate of iron is 100%, and the leaching rate of gold and silver is over 98%. The extract was filtered, the temperature of the system was lowered to room temperature, and then filtered. The filtrate is neutralized with alkali until the pH value is 1.5, and the flocculant polyacrylamide is added to remove the precipitate, and the co-solvent is separated, and then ammonia water is added at 90°C until the iron ions are completely precipitated. After filtration, the filtrate is used to recover ammonia water and alkali, and the filter residue is washed, dried and ...
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