KR desulfurizing agent, preparation method thereof and desulfurizing method adopting desulfurizing agent
A desulfurizing agent and desulfurizing molten iron technology, applied in the field of steelmaking, can solve the problems of high effluent cost, difficulty in LT ash digestion, etc., and achieve the effects of reducing production cost, promoting desulfurization effect, and improving metal yield
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[0045]The present invention provides a kind of preparation method of KR desulfurizer, described preparation method comprises: CaO powder and LT ash (the described LT ash is converter dry dedusting ash) is mixed;
[0046] Wherein, the mass ratio of the CaO powder and the LT ash is (3.5-4):(1.5-1);
[0047] In terms of mass percentage, the LT ash contains: TFe 55%-65%, CaO≤5%, MnO≤0.03%, MgO≤2%.
[0048] In one embodiment, in the preparation method of the KR desulfurizer described in the present invention, the particle diameter of the CaO powder is 0.2-1mm;
[0049] In a preferred embodiment, in the preparation method of the KR desulfurizer described in the present invention, in the CaO powder, in terms of mass percentage, particles with a particle diameter of 0.2-1mm ≥ 80%, particles with a particle diameter of less than 0.2mm Particles ≤ 10%, particles with a particle size greater than 1mm ≤ 10%.
[0050] In one embodiment, in the preparation method of the KR desulfurizer de...
Embodiment 1
[0072] In this embodiment, the preparation method of the KR desulfurizer is: mix the CaO powder and the LT ash at a mass ratio of 3.5:1.5. Wherein, in terms of mass percentage, the LT ash contains: TFe 55%-65%, CaO≤5%, MnO≤0.03%, MgO≤2%;
[0073] In the CaO powder, by mass percentage, the particles with a particle diameter of 0.2-1mm are ≥80%, the particles with a particle diameter of less than 0.2mm are ≤10%, and the particles with a particle diameter of more than 1mm are ≤10%; the particle size of the LT ash is The diameter is 50~65um;
[0074] According to the present invention, the desulfurization method includes mixing the CaO powder and LT ash with 238t (tons) of molten iron to be desulfurized at a temperature of 1300°C; wherein, the mass ratio of CaO powder to LT ash is 3.5: 1.5; CaO powder and The ratio of the mass sum of LT ash to the mass of the above-mentioned molten iron to be desulfurized is 6:900;
[0075] Specifically, including:
[0076] (1) The CaO powder a...
Embodiment 2
[0081] In the present embodiment, the preparation method of the KR desulfurizer is: mixing the CaO powder and the LT ash with a mass ratio of 4:1;
[0082] Wherein, by mass percentage, the LT ash contains: TFe 55%-65%, CaO≤5%, MnO≤0.03%, MgO≤2%; in the KR desulfurizer, the CaO powder and the LT The mass ratio of ash is 4:1;
[0083] In the CaO powder, by mass percentage, the particles with a particle diameter of 0.2-1mm are ≥80%, the particles with a particle diameter of less than 0.2mm are ≤10%, and the particles with a particle diameter of more than 1mm are ≤10%; the particle size of the LT ash is The diameter is 5~76.4um;
[0084] According to the present invention, the desulfurization method includes mixing the CaO powder and LT ash with 238t (tons) of molten iron to be desulfurized at a temperature of 1400°C, wherein the mass ratio of CaO powder and LT ash is 4:1; CaO powder and The ratio of the mass sum of LT ash to the mass of the molten iron to be desulfurized is 7:1...
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