Multi-stage suspension magnetizing roasting-magnetic separation system device and method for refractory iron ore
US-10543491-B2 · Jan 28, 2020 · US
US2024052442A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024052442-A1 |
| Application number | US-202118250928-A |
| Country | US |
| Kind code | A1 |
| Filing date | Oct 28, 2021 |
| Priority date | Oct 30, 2020 |
| Publication date | Feb 15, 2024 |
| Grant date | — |
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A process for steel production that includes: production of sponge iron from iron oxide-containing starting material by direct reduction with reduction gas, wherein the reduction gas has at least 20% by volume of hydrogen H 2 , and production of an iron melt having a carbon content of 1-5% by mass from the sponge iron. Sponge iron is subjected to a treatment that includes: energy input and addition of additives to produce a melt and a slag, wherein the energy input is effected substantially from electricity and wherein the slag has a basicity B2 of less than 1.3, preferably less than 1.25, particularly preferably less than 1.2, adjustment of the carbon content in the melt, reduction of at least a sub-amount of the iron oxides present in the sponge iron The slag is separated during and/or after the treatment.
Opening claim text (preview).
1 . A process for steel production comprising production of sponge iron from iron oxide-containing starting material by direct reduction with reduction gas, wherein the reduction gas comprises at least 20% by volume of hydrogen H2, and production of an iron melt having a carbon content of 1-5% by mass, wherein at least a sub-amount of the sponge iron produced from iron oxide-containing starting material by direct reduction with reduction gas is subjected to a treatment, wherein the treatment comprises: energy input and addition of additives to produce a melt and a slag wherein the energy input is effected substantially from electricity and wherein the slag has a basicity B2 of less than 1.3, preferably less than 1.25, particularly preferably less than 1.2, adjustment of the carbon content in the melt, reduction of at least a sub-amount of the iron oxides present in the sponge iron and wherein the slag is separated during and/or after the treatment and use of the iron melt for production of steel. 2 . The process as claimed in claim 1 , wherein the direct reduction is performed using a reduction gas comprising more than 45% by volume of hydrogen H2. 3 . The process as claimed in claim 1 , wherein the direct reduction is carried out in a direct reduction reactor the treatment is carried out in a treatment reactor and the direct reduction reactor and the treatment reactor are spatially separate from one another. 4 . The process as claimed in claim 1 , wherein the energy input is effected via an electric arc. 5 . The process as claimed in claim 1 , wherein the energy input is effected via electric resistance heating. 6 . The process as claimed in claim 1 , wherein the energy input is effected via a hydrogen plasma produced using electricity. 7 . The process as claimed in claim 1 , wherein the energy input is effected partly via introduction of oxygen for gasification of carbon supplied to the melt in the solid or liquid state or of carbon dissolved in the melt. 8 . The process as claimed in claim 1 , wherein the adjustment of the carbon content in the melt is effected using supplied carbon carriers. 9 . The process as claimed in claim 1 , wherein the adjustment of the carbon content in the melt is effected using supplied oxygen. 10 . The process as claimed in claim 1 , wherein the reduction of at least a sub-amount of the iron oxides present in the sponge iron is effected using supplied carbon carriers. 11 . The process as claimed in claim 1 , wherein the reduction of at least a sub-amount of the iron oxides present in the sponge iron is effected using carbon present in the sponge iron. 12 . The process as claimed in claim 1 , wherein the reduction of at least a sub-amount of the iron oxides present in the sponge iron is effected at least partly using electric current. 13 . The process as claimed in claim 1 , wherein the treatment effects a lowering of the melting range using supplied solid carbon carriers and/or liquid carbon carriers and/or gaseous carbon carriers. 14 . The process as claimed in claim 1 , wherein the production of steel employs the LD/BOF process.
Multi-stage processes {processes carried out in different vessels or furnaces} · CPC title
Selection or treatment of the reducing gases · CPC title
in a plasma heated furnace · CPC title
Injection of partially reduced ore into a molten bath · CPC title
Treatment with gases (C21C7/06, C21C7/064, C21C7/068 take precedence) · CPC title
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