A method for simultaneously preparing sulfuric acid and potassium sulfate by utilizing potassium feldspar, phosphogypsum, and silica
A technology of potassium feldspar and phosphogypsum, applied in the field of chemical metallurgy, can solve the problems of low sulfur recovery rate, achieve high decomposition rate, increase ash melting point, and high recovery rate
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Embodiment 1
[0017] (1) Mix potassium feldspar finely ground to below 150 μm with phosphogypsum and silica at a mass ratio of 1:4:2;
[0018] (2) The mixture is mixed with sodium humate as a binder for pelletizing;
[0019] (3) Roast the pellets at 1200 °C for 120 min to obtain solid reduction products and 2 exhaust;
[0020] (4) leaching the solid reduction product obtained in step (3) with water to obtain a potassium-rich solution, the leaching temperature is 90°C, the leaching time is 60min, and the liquid-solid mass ratio is 2:1; by analyzing the potassium content in the potassium-rich solution, Calculation and the ratio of the potassium element in the obtained potassium feldspar, the extraction rate of available potassium is 86%; the decomposition rate of phosphogypsum is 98%;
[0021] (5) with the SO containing SO obtained in step (3) 2 After the tail gas is dedusted and purified, it is sent to the sulfuric acid system to prepare the finished sulfuric acid product.
Embodiment 2
[0023] (1) Evenly mix potassium feldspar finely ground to below 150 μm with phosphogypsum and silica at a mass ratio of 1:2:1;
[0024] (2) The mixture is mixed with sodium humate as a binder for pelletizing;
[0025] (3) Roast the pellets at 1150°C for 240 min to obtain solid reduction products and 2 exhaust;
[0026] (4) leaching the solid reduction product obtained in step (3) with water to obtain a potassium-rich solution, the leaching temperature is 40°C, the leaching time is 120min, and the liquid-solid mass ratio is 3:1; by analyzing the potassium content in the potassium-rich solution, Calculation and the ratio of the potassium element in the obtained potassium feldspar, the extraction rate of available potassium is 75%; the decomposition rate of phosphogypsum is 87%;
[0027] (5) with the SO containing SO obtained in step (3) 2 After the tail gas is dedusted and purified, it is sent to the sulfuric acid system to prepare the finished sulfuric acid product.
Embodiment 3
[0029] (1) Mix potassium feldspar finely ground to below 150 μm with phosphogypsum and silica at a mass ratio of 1:4:1;
[0030] (2) The mixture is mixed with sodium humate as a binder for pelletizing;
[0031] (3) Roast the pellets at 1300 °C for 30 min to obtain solid reduction products and SO-containing 2 exhaust;
[0032] (4) leaching the solid reduction product obtained in step (3) with water to obtain a potassium-rich solution, the leaching temperature is 60°C, the leaching time is 30min, and the liquid-solid mass ratio is 4:1; by analyzing the potassium content in the potassium-rich solution, Calculation and the ratio of the potassium element in the potassium feldspar obtained, the extraction rate of available potassium is 81%; the decomposition rate of phosphogypsum is 93%;
[0033] (5) with the SO containing SO obtained in step (3) 2 After the tail gas is dedusted and purified, it is sent to the sulfuric acid system to prepare the finished sulfuric acid product.
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