Mixture, use of this mixture, and method for conditioning a slag located on a metal melt in a metallurgical vessel in iron and steel metallurgy
US-2017275714-A1 · Sep 28, 2017 · US
US2024246145A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024246145-A1 |
| Application number | US-202118287106-A |
| Country | US |
| Kind code | A1 |
| Filing date | Apr 21, 2021 |
| Priority date | Apr 21, 2021 |
| Publication date | Jul 25, 2024 |
| Grant date | — |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A process for the production of steel powders including the steps of: providing molten iron from a blast furnace, refining the molten iron in a converter to form molten steel, refining the molten steel in a vacuum arc degasser to obtain a refined molten steel comprising from 20 to less than 600 ppm C, from 15 to less than 120 ppm S, up to 125 ppm P, up to 80 ppm N and up to 30 ppm O, pouring in a plurality of induction furnaces, adding at least one ferroalloy, pouring the molten steel of each induction furnace in a dedicated reservoir connected to at least one gas atomizer, feeding the at least one gas atomizer of each reservoir in molten steel from each reservoir under pressure and gas atomizing the molten steel to form the steel powder at the desired composition.
Opening claim text (preview).
What is claimed is: 1 - 23 . (canceled) 24 . A process for the production of steel powders comprising the steps of: providing molten iron from a blast furnace; refining the molten iron in a converter to form molten steel comprising up to 600 ppm C, up to 120 ppm S, up to 125 ppm P, up to 50 ppm N and up to 1200 ppm O; refining the molten steel in a vacuum arc degasser to obtain a refined molten steel comprising from 20 to less than 600 ppm C, from 15 to less than 120 ppm S, up to 125 ppm P, up to 80 ppm N and up to 30 ppm O; pouring the refined molten steel in a plurality of induction furnaces; adding, in each of the plurality of induction furnaces, at least one ferroalloy to adjust the steel composition to the one of the desired steel powder; pouring the molten steel at the desired composition of each induction furnace in a dedicated reservoir connected to at least one gas atomizer; and feeding the at least one gas atomizer of each reservoir in molten steel from each reservoir under pressure and gas atomizing the molten steel to form the steel powder at the desired composition. 25 . The process as recited in claim 24 wherein the molten steel comprises up to 250 ppm C and/or up to 90 ppm P and/or up to 25 ppm N. 26 . The process as recited in claim 24 wherein, during the refinement in the vacuum arc degasser, molten steel is decarburized by using dissolved oxygen in steel. 27 . The process as recited in claim 24 wherein, during the refinement in the vacuum arc degasser, molten steel is deoxidized until the dissolved O content is lower than or equal to 4 ppm. 28 . The process as recited in claim 24 wherein, during the refinement in the vacuum arc degasser, molten steel is desulphurized by stirring the slag against the steel. 29 . The process as recited in claim 24 wherein the temperature of the refined molten steel at the end of the refinement in the vacuum arc degasser is between 1580 and 1680° C. 30 . The process as recited in claim 24 wherein the refined molten steel is directly poured from the vacuum arc degasser to the plurality of induction furnaces. 31 . The process as recited in claim 24 wherein the refined molten steel is first poured in a tundish and then poured from the tundish to the plurality of induction furnaces. 32 . The process as recited in claim 31 wherein the tundish is capable of simultaneously pouring the refined molten steel in all the induction furnaces. 33 . The process as recited in claim 31 wherein the temperature in the tundish is maintained between 1520 and 1620° C. 34 . The process as recited in claim 31 wherein the tundish is purged with Argon to control the oxygen content in the tundish. 35 . The process as recited in claim 24 wherein the temperature in the plurality of induction furnaces is maintained between 1500 and 1700° C. 36 . The process as recited in claim 35 wherein the temperature in at least one of the plurality of induction furnaces is maintained between 1620 and 1650° C. 37 . The process as recited in claim 24 wherein the ferroalloy added in the induction furnaces is not pre-melted. 38 . The process as recited in claim 24 wherein scraps or Direct Reduced Iron or silicide alloys or nitride alloys or pure elements or a mixture thereof are added in at least one of the plurality of induction furnaces. 39 . The process as recited in claim 24 wherein the induction furnaces are not atmospherically controlled. 40 . The process as recited in claim 24 wherein at least one of the plurality of induction furnaces is a vacuum induction furnace. 41 . The process as recited in claim 24 wherein the atmosphere in each of the dedicated reservoirs is Argon, Nitrogen or a mixture thereof. 42 . The process as recited in claim 24 wherein the temperature in each of the dedicated reservoirs is maintained between 1300 and 1750° C. 43 . The process as recited in claim 24 wherein the temperature in each of the dedicated reservoirs is at least 150° ° C. above the liquidus temperature of the molten steel. 44 . An installation for the production of steel powders comprising: a blast furnace; a converter capable of refining molten iron and form molten steel comprising up to 600 ppm C, up to 120 ppm S, up to 125 ppm P, up to 50 ppm N and up to 1200 ppm O; a vacuum arc degasser capable of refining molten steel to obtain a refined molten steel comprising from 20 to less than 600 ppm C, from 15 to less than 120 ppm S, up to 125 ppm P, up to 80 ppm N and up to 30 ppm O; a plurality of induction furnaces; a ferroalloy feeding unit capable of feeding the plurality of induction furnaces in at least one ferroalloy; and a dedicated reservoir to each induction furnace, each dedicated reservoir being connected to at least one gas atomizer and capable of being pressurized. 45 . The installation as recited in claim 44 further comprising a tundish capable of simultaneously pouring the molten steel in all the induction furnaces. 46 . The installation as recited in claim 45 the tundish is positioned above the plurality of induction furnaces.
Dephosphorising; Desulfurising · CPC title
Melting process before atomisation · CPC title
Use of slags or fluxes as treating agents (C21C7/06, C21C7/064, C21C7/068 take precedence) · CPC title
casting construction of the melt process, apparatus, intermediate reservoir, e.g. tundish, devices for temperature control · CPC title
Deoxidising, e.g. killing · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.