Method for treatment of chrome-containing molten iron and slag
Chrome-containing molten iron and slag are to be obtained in an electric furnace operation using CaF 2 -free slag. In order to reduce and collect chrome from the slag while simultaneously promoting desulfurization of molten iron, a chrome-containing molten iron produced in an electric furnace and having a Cr content of from 8.0 to 35.0% by mass, and a CaF 2 -free electric furnace slag formed during the molten iron production, including Cr 2 O 3 , SiO 2 and CaO as the constituent components and having a basicity CaO/SiO 2 of from 0.7 to 1.7, are mechanically stirred with an impeller in a refining vessel. A metal Al-containing substance and CaO are put into the vessel before the end of stirring to thereby control the basicity of the slag after the end of stirring to at least 1.9
1. A method for treatment of chrome-containing molten iron and slag,
Comprising mechanically stirring a chrome-containing molten iron produced in an electric furnace and having a Cr content of from 8.0 to 35.0% by mass, and a Ca F2-free electric furnace slag formed during the molten iron production including Cr 2 O 3 , SiO 2 and CaO as constituent components and having a basicity CaO/SiO 2 of from 0.7 to 1.7, with an impeller in a refining vessel,
wherein a metal Al-containing substance, which is a reducing agent of Cr 2 O 3 , and CaO are put into the vessel before the end of stirring to thereby control the basicity of the slag after the end of stirring to at least 1.9.
2. The method for treatment of chrome-containing molten iron and slag as claimed in claim 1 , wherein the metal Al-containing substance is aluminum dross containing a metal Al in an amount of from 20 to 80% by mass.
3. The method for treatment of chrome-containing molten iron and slag as claimed in claim 1 , wherein the basicity of the slag after the end of stirring is controlled to from 1.9 to 3.0.
4. The method for treatment of chrome-containing molten iron and slag as claimed in claim 1 , wherein the basicity of the slag after the end of stirring is controlled to from 2.0 to 3.0.