The 18 TPH capacity matches the steel mill’s daily desulfurization demand (432 tons per day).​

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Grinding System Design​
 
The project uses a ball mill with a length of 8 meters and a diameter of 2.4 meters—chosen for its ability to handle mixed minerals with varying hardness (dolomite Mohs hardness 3.5-4, calcium carbonate Mohs hardness 3). The ball mill is filled with high-chromium steel balls (diameters 50-80mm) at a filling rate of 35%, which provides optimal grinding efficiency. The blended material is fed into the mill via a screw conveyor, and the mill operates at a rotational speed of 21 rpm—fast enough to lift the balls but slow enough to avoid excessive wear.​
 
To control fineness, the ball mill is paired with an air classifier (installed at the mill’s discharge end). The classifier uses a variable-speed impeller (1500-2000 rpm) to separate particles: 200-mesh particles are carried by air to a pulse bag filter, while coarser particles return to the mill for regrinding. A fan maintains negative pressure in the system, preventing dust leakage and ensuring efficient particle transport. The pulse bag filter has 240 filter bags, each with a surface area of 2 m², achieving a dust collection efficiency of 99.95%.​
 
Post-Processing and Storage​
 
The collected 200-mesh powder is conveyed to a rotary dryer (heated by waste heat from the steel mill’s flue gas) to reduce moisture content to <0.5%—moisture can cause powder agglomeration and reduce desulfurization efficiency. The dried powder is then sent to a 1000-ton silo, equipped with level sensors to monitor inventory. From the silo, the powder is transported to the steel mill via a sealed pipeline (1.2 meters in diameter) using compressed air, avoiding dust pollution during transportation.​