Elaboration of an advanced ceramic made of recycled industrial steel waste
US-11787745-B2 · Oct 17, 2023 · US
US10174389B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10174389-B2 |
| Application number | US-201415038514-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 27, 2014 |
| Priority date | Nov 28, 2013 |
| Publication date | Jan 8, 2019 |
| Grant date | Jan 8, 2019 |
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A method for treating desulfurization slag involves conveying desulfurization slag from pig iron desulfurization to a unit where the desulfurization slag is melted at a temperature of at least 1,400° C. In the unit, a thorough mixing is achieved. The treatment takes place in the unit under oxidizing conditions. Sulfur dioxide is generated and collected from the roasting gas and supplied for further utilization.
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The invention claimed is: 1. A method for treating desulfurization slag, comprising: (a) providing desulfurization slag comprising sulfur, from pig iron desulfurization, (b) conveying said desulfurization slag to a unit including a burner, said unit assuring a thorough mixing, (c) melting the desulfurization slag at a temperature of at least 1,400° C., wherein a λ value of the burner is set to 1.3-1.6 during said melting, (d) setting the burner to a λ value greater than 2.0 to generate a roasting gas including SO 2 , (e) collecting the generated SO 2 , and (f) supplying said generated SO 2 for further utilization. 2. The method of claim 1 , further comprising adding quicklime to the desulfurization slag in the unit. 3. The method of claim 1 , further comprising tapping of a treated desulfurization slag and feeding the treated desulfurization slag into pig iron production. 4. The method of claim 3 , wherein the treated desulfurization slag has a sulfur content of less than 0.1% by mass. 5. The method of claim 3 , wherein the treated desulfurization slag has a sulfur content of less than 0.01% by mass. 6. The method of claim 1 , wherein the unit is a top blown rotary converter. 7. The method of claim 1 , wherein the λ value of the burner during melting is set to 1.4-1.5. 8. The method of claim 7 , further comprising adding quicklime to the desulfurization slag in the unit. 9. The method of claim 7 , further comprising tapping of a treated desulfurization slag and feeding the treated desulfurization slag into pig iron production. 10. The method of claim 7 , wherein a treated desulfurization slag has a sulfur content of less than 0.1% by mass. 11. The method of claim 7 , wherein a treated desulfurization slag has a sulfur content of less than 0.01% by mass. 12. The method according to claim 1 , wherein the unit is a top blown rotary converter. 13. A method for treating desulfurization slag, comprising: (a) providing desulfurization slag comprising sulfur, from pig iron desulfurization, (b) conveying said desulfurization slag to a unit including a burner, said unit assuring a thorough mixing, (c) melting the desulfurization slag at a temperature of at least 1,400° C., wherein a λ value of the burner is set to 1.3-1.6 during said melting, (d) setting the burner to a λ value greater than 2.0 to generate a roasting gas including SO 2 , CO and dust, (e) afterburning at a temperature of at least 800° C., (f) cooling the roasting gas, (g) collecting the generated SO 2 , (h) removing the dust, and (i) supplying said generated SO 2 for further utilization. 14. The method of claim 13 , further comprising adding quicklime to the desulfurization slag in the unit. 15. The method of claim 13 , further comprising tapping of a treated desulfurization slag and feeding the treated desulfurization slag into pig iron production. 16. The method of claim 13 , wherein a treated desulfurization slag has a sulfur content of less than 0.1% by mass. 17. The method of claim 13 , wherein a treated desulfurization slag has a sulfur content of less than 0.01% by mass. 18. The method according to claim 13 , wherein the unit is a top blown rotary converter. 19. The method according to claim 13 , further comprising: (a) determining a volume percent of exhaust gas components CO and SO 2 in an exhaust gas during the melting of the slag and during generating the roasting gas, (b) when the volume ratio of SO 2 to CO exceeds unity, setting the burner λ value to greater than 2. 20. The method of claim 19 , further comprising adding quicklime to the desulfurization slag in the unit.
Dephosphorising or desulfurising · CPC title
Sulphur removal · CPC title
Treatment of liquid slag · CPC title
Working-up slag · CPC title
Treatment of {metallurgical} slag (manufacture of slag wool C03B; in, or for, the production of metals C21B, C22B); Artificial stone from molten {metallurgical} slag {(other cast stone C04B32/005; mechanical aspects B28B1/54)} · CPC title
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