Desulphurization of ferrous materials using glass cullet
a technology of ferrous materials and glass cullets, which is applied in the direction of furnace details, crucible furnaces, furnaces, etc., can solve the problems of undesirable sulphur above 0.015%, ineffective desulphurizing effect of metallic sodium, and inability to replace sulphur, so as to improve the effect of desulphurization and control of the fluidity of spent reactants
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example 1
[0018] A reactive desulphurization agent, based on sodium, was prepared from a glass cullet and oxides of aluminum, magnesium and calcium. The glass cullet had a silicon oxide to the sodium oxide parts ratio composition of 2.3:1, resulting in about 29.7%, by weight, of sodium oxide and about 71.3%, by weight, of silicon oxide. In addition to the glass cullet composition, anhydrous calcined materials: alumina, dolomite and lime, where added in the amounts given in Table 1. The components where combined using a blade mixer in three approximately equal batches to obtain consistent mixtures. The percentages based on weight (pbw) of the oxides for the unspent reactive desulphurizing agent are listed in Table 2. After mixing, the components were placed super-sacks and shipped to the site of the Basic Oxygen Furnace (BOF).
TABLE 1Desulphurizing AgentComponent WeightComponentKgGlass cullet234.5Alumina284.1Dolomite218.8Lime535.4Total1272.8
[0019]
TABLE 2Desulphurizing Agent Composition (pbw)P...
example 2
[0021] In the second example, the sodium-based reactive desulphurizing agent based was again prepared from a glass cullet and oxides of aluminum, magnesium and calcium. The parts ratio of the silicon oxide to the sodium oxide was maintained as before, 2.3:1, resulting in a glass cullet composition with about 29.7%, by weight, of sodium oxide and about 71.3%, by weight, of silicon oxide. However the amounts the glass cullet composition, and the three anhydrous calcined materials: alumina, dolomite and lime, were slightly changed, as given by weight amounts in Table 3. As before, the components where combined using a blade mixer in successive separate batches. The individual batch weights for this example were not reported. The percentages based on weight of the oxide in the final sodium-based reactive desulphurizing agent composition are listed in Table 4. After mixing, the components were placed super-sacks and shipped to the BOF site.
TABLE 3Desulphurizing AgentComponent WeightCom...
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