Method for preparing manganese sulfate from oil refining waste acid
A technology of manganese sulfate and manganese oxide ore, applied in the direction of manganese sulfate, etc., can solve problems such as cost increase, and achieve the effects of reducing environmental protection pressure, low cost, and comprehensive utilization of resources
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Embodiment 1
[0022] Add 140g oil refining waste acid to 320g water, add 98g manganese oxide ore, Mn in manganese oxide ore 4+ The content is 29.24%, and the reaction temperature is above 95°C. Slowly add 420g of qualified concentrated sulfuric acid during the reaction to maintain the reaction acidity at 5-6. After 6 hours of reaction, add 2500mL washing liquid and 1100g of manganese oxide roasting material. 2+ The content is 30.38%. After reacting for 2 hours, filter the leaching slag and leaching solution. The specific gravity of the leaching solution is 45 Baume. The water is treated and stacked; the leachate is crystallized to obtain crystallized mother liquor and crystallized MnSO 4 , where the Mn content is 32.18%, the crystallization mother liquor is returned to immerse manganese, and the crystallization of MnSO 4 After drying and crushing, it is packaged to form a qualified manganese sulfate finished product.
Embodiment 2
[0024] Add 260g oil refining waste acid to 600g water, add 182g manganese oxide ore, Mn in manganese oxide ore 4+ The content is 29.24%, and the reaction temperature is above 95°C. Slowly add 260g of qualified concentrated sulfuric acid to maintain the reaction acidity of 5-6 during the reaction. 2+ The content is 30.38%, add 60g CaCO 3 Neutralize with the acid in the solution to reduce the acidity. After reacting for 2 hours, filter to obtain leaching residue and leaching solution. The specific gravity of the leaching solution is 32 Baume. Wash the leaching residue with 10g / L sulfuric acid and water to obtain the lotion and leaching residue, and return the lotion to leaching Manganese, washing slag is treated with lime water and piled up; leaching solution is crystallized to obtain crystalline mother liquor and crystalline MnSO 4 , where the Mn content is 32.12%, the crystallization mother liquor is returned to immerse manganese, and the crystallization of MnSO 4 After dryi...
Embodiment 3
[0026] Add 140g oil refinery waste acid to 320g water, add 98g electrolytic manganese anode slag, the Mn in the anode slag 4+ The content is 45%, and the reaction temperature is above 95°C. Slowly add 420g of qualified concentrated sulfuric acid during the reaction to maintain the reaction acidity of 5-6. After 6 hours of reaction, add 3000mL of washing liquid, 1100g of manganese oxide roasting material, and the Mn in the manganese oxide roasting material 2+ The content is 30.38%. After reacting for 2 hours, the leach slag and leachate are obtained by filtering. The specific gravity of the leachate is 43 Baume. 38.27%, as lead concentrate product; crystallization of leaching solution to obtain crystallization mother liquor and crystallization MnSO 4 , where the Mn content is 32.22%, the crystallization mother liquor is returned to immerse manganese, and the crystallization of MnSO 4 After drying and crushing, it is packaged to form a qualified manganese sulfate finished produ...
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