BE1009828A3 - Method of recovering iron-rich iron and steel manufacturing residues - Google Patents
Method of recovering iron-rich iron and steel manufacturing residues Download PDFInfo
- Publication number
- BE1009828A3 BE1009828A3 BE9500623A BE9500623A BE1009828A3 BE 1009828 A3 BE1009828 A3 BE 1009828A3 BE 9500623 A BE9500623 A BE 9500623A BE 9500623 A BE9500623 A BE 9500623A BE 1009828 A3 BE1009828 A3 BE 1009828A3
- Authority
- BE
- Belgium
- Prior art keywords
- charge
- iron
- reduction
- oxides
- residues
- Prior art date
Links
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims abstract description 26
- 229910000831 Steel Inorganic materials 0.000 title claims abstract description 19
- 239000010959 steel Substances 0.000 title claims abstract description 19
- 229910052742 iron Inorganic materials 0.000 title claims abstract description 13
- 238000000034 method Methods 0.000 title claims description 22
- 238000004519 manufacturing process Methods 0.000 title description 11
- 239000002893 slag Substances 0.000 claims abstract description 23
- 230000009467 reduction Effects 0.000 claims abstract description 14
- 229910052751 metal Inorganic materials 0.000 claims abstract description 13
- 239000002184 metal Substances 0.000 claims abstract description 13
- 239000000203 mixture Substances 0.000 claims abstract description 12
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 7
- 229910052500 inorganic mineral Inorganic materials 0.000 claims abstract description 7
- 239000011707 mineral Substances 0.000 claims abstract description 7
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 6
- 239000000126 substance Substances 0.000 claims abstract description 6
- 150000001875 compounds Chemical class 0.000 claims abstract description 4
- 230000003750 conditioning effect Effects 0.000 claims abstract description 4
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims abstract description 4
- 235000013980 iron oxide Nutrition 0.000 claims abstract description 4
- VBMVTYDPPZVILR-UHFFFAOYSA-N iron(2+);oxygen(2-) Chemical class [O-2].[Fe+2] VBMVTYDPPZVILR-UHFFFAOYSA-N 0.000 claims abstract description 4
- 229910052681 coesite Inorganic materials 0.000 claims abstract description 3
- 229910052906 cristobalite Inorganic materials 0.000 claims abstract description 3
- 229910052682 stishovite Inorganic materials 0.000 claims abstract description 3
- 229910052905 tridymite Inorganic materials 0.000 claims abstract description 3
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims abstract 5
- 235000010755 mineral Nutrition 0.000 claims abstract 2
- 238000002844 melting Methods 0.000 claims description 10
- 230000008018 melting Effects 0.000 claims description 10
- 239000003638 chemical reducing agent Substances 0.000 claims description 5
- 229910001338 liquidmetal Inorganic materials 0.000 claims description 2
- 239000000945 filler Substances 0.000 claims 1
- 230000004927 fusion Effects 0.000 claims 1
- 229910000027 potassium carbonate Inorganic materials 0.000 abstract description 3
- 239000000377 silicon dioxide Substances 0.000 abstract description 3
- 235000012239 silicon dioxide Nutrition 0.000 abstract description 2
- 238000003723 Smelting Methods 0.000 abstract 1
- 235000015320 potassium carbonate Nutrition 0.000 abstract 1
- 235000011181 potassium carbonates Nutrition 0.000 abstract 1
- 239000000428 dust Substances 0.000 description 12
- 238000006722 reduction reaction Methods 0.000 description 9
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 4
- 229910052725 zinc Inorganic materials 0.000 description 4
- 239000011701 zinc Substances 0.000 description 4
- 239000010802 sludge Substances 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000010902 straw Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 229910001021 Ferroalloy Inorganic materials 0.000 description 1
- 229910000604 Ferrochrome Inorganic materials 0.000 description 1
- 229910000863 Ferronickel Inorganic materials 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 229910000805 Pig iron Inorganic materials 0.000 description 1
- 239000011398 Portland cement Substances 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000001722 carbon compounds Chemical class 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- -1 silica or alumina Chemical class 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
- C22B7/04—Working-up slag
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C1/00—Refining of pig-iron; Cast iron
- C21C1/02—Dephosphorising or desulfurising
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/56—Manufacture of steel by other methods
- C21C5/562—Manufacture of steel by other methods starting from scrap
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/04—Removing impurities by adding a treating agent
- C21C7/06—Deoxidising, e.g. killing
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/04—Removing impurities by adding a treating agent
- C21C7/064—Dephosphorising; Desulfurising
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
- C22B7/02—Working-up flue dust
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Mechanical Engineering (AREA)
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
A load containing iron-rich residues, particularly at least one steel slag, is smelted and the molten load is subjected to a reduction step of at least one part of the oxides that it contains to form a raw metal. Smelting and reduction may be carried out in a single step. The load may additionally contain a corrective substance, containing at least one oxidised compound chosen according to the use planned for the mineral phase resulting from the reduction operation. The raw metal is subjected to a conditioning step including a dephosphorisation operation, preferably by means of a dephosphorisation slag including iron oxides Fe203, a mixture of oxides CaO and SiO2 and a fluxing agent, particularly potassium carbonate K2CO3.
Description
<Desc/Clms Page number 1>
EMI1.1
Procédé de valorisation de résidus sidérurgiques riches en fer.
La présente invention concerne un procédé de valorisation de résidus sidérurgiques riches en fer, tels que des scories et des poussières d'aciéries et de hauts-fourneaux.
Les différentes étapes de la fabrication d'un produit sidérurgique s'accompagnent de la production de quantités variables, parfois importantes, de résidus divers. Nombre de ces résidus contiennent des quantités appréciables de fer, généralement sous forme d'oxydes, qui sont perdues pour le processus de fabrication en cours. Ces résidus sont, par exemple, les poussières et les boues de hauts-fourneaux, les scories, les poussières et les boues d'aciéries, les pailles de laminoirs et les boues de décapage.
Il existe actuellement de nombreux procédés destinés à valoriser l'un ou l'autre type de résidu, tant à l'intérieur qu'à l'extérieur des usines sidérurgiques. Par exemple, on utilise certaines scories d'aciéries en agriculture et on recycle certaines poussières riches en fer, sous différentes formes, au four électrique d'aciérie. Le recyclage de poussières riches en fer se complique cependant souvent en raison de la présence de zinc, à des teneurs variables, dans ces poussières, en particulier les poussières de hauts-fourneaux.
Il est fréquent que les procédés de recyclage génèrent à leur tour des résidus qui doivent finalement soit être à leur tour recyclés, éventuellement hors de l'industrie sidérurgique, soit être mis en décharge, parce qu'il n'existe pour eux aucun débouché intéressant.
La présente invention a pour objet de proposer un procédé de valorisation de résidus sidérurgiques riches en fer, qui vise à créer, pour l'industrie sidérurgique, une situation de"zéro déchet", dans laquelle tout produit obtenu par les opérations sidérurgiques peut trouver une réelle utilisation.
Conformément à la présente invention, un procédé de valorisation de résidus sidérurgiques riches en fer, est caractérisé en ce que l'on fond une charge contenant
<Desc/Clms Page number 2>
lesdits résidus, en ce que l'on soumet ladite charge fondue à une étape de réduction d'au moins une partie des oxydes qu'elle contient pour former un métal brut, et en ce que l'on soumet ledit métal brut à une étape de conditionnement comprenant une opération de déphosphoration.
Il va de soi que la charge contenant lesdits résidus peut se trouver initialement, au moins en partie, à l'état fondu.
Selon une mise en oeuvre particulière, la fusion et la réduction de la charge peuvent être effectuées en une seule étape.
La charge est constituée par un mélange composé de résidus riches en fer, tels que ceux qui ont été mentionnés plus haut. De préférence, ces résidus comprennent au moins une scorie d'aciérie.
Avant et/ou pendant l'étape de réduction, on ajoute à la charge un agent réducteur, qui est de préférence un composé carboné.
Si la fusion et la réduction sont effectuées en une seule étape, il est avantageux que la charge contienne initialement au moins une partie de l'agent réducteur requis.
D'une façon générale, le mélange constituant la charge peut être réalisé suivant toute manière appropriée, par exemple en enfournant séparément les différents constituants du mélange dans le four de fusion ou de fusion et de réduction. Il peut cependant s'avérer intéressant de réaliser ce mélange à l'extérieur du four, de façon à garantir la précision de sa composition ainsi que son homogénéité, et de le charger ensuite dans le four.
Les résidus constituant la charge peuvent contenir des oxydes de fer, mais aussi des oxydes ou d'autres composés présents dans les scories d'aciéries. De même, des poussières incorporées au mélange peuvent y introduire d'autres métaux, par exemple du zinc ou du plomb provenant des poussières de hauts-fourneaux.
<Desc/Clms Page number 3>
Le métal brut obtenu à partir de résidus riches en fer du type précité est généralement une fonte brute, utilisable pour la fabrication d'un acier au carbone, principalement dans un four électrique.
Suivant une variante intéressante, les résidus comprennent des scories et/ou des poussières riches en chrome et/ou en nickel. Une charge contenant de tels résidus sera de préférence traitée séparément ; le métal brut obtenu dans ces conditions peut notamment être utilisé pour la fabrication de ferro-alliages tels que du ferrochrome ou du ferronickel.
L'agent réducteur utilisé est de préférence un agent carboné finement divisé, en particulier du charbon pulvérisé ; sa combustion contribue non seulement au chauffage et à la fusion de la charge, mais assure aussi la production de gaz réducteur, notamment de CO, pour la réduction des oxydes.
Le chauffage de la charge peut être assuré par tout moyen approprié, notamment par combustion d'une substance combustible, par voie électrique ou par toute combinaison de ces deux techniques. Outre la fusion de la charge et la production de gaz réducteur, il peut aussi provoquer la vaporisation de certains composants comme le plomb ou le zinc introduits notamment par les poussières de hauts-fourneaux ; on peut ainsi produire une vapeur de zinc fortement concentrée, aisément valorisable.
Enfin, la charge peut contenir une substance minérale, dite de correction, dont la composition est choisie en fonction d'une part de la composition des matières minérales de départ et d'autre part de celle de la phase minérale finale désirée en fonction de l'utilisation envisagée.
Cette substance minérale peut notamment être constituée de composés oxydés, tels que la silice ou l'alumine, qui sont présents dans les scories d'aciéries. On peut également utiliser des cendres d'incinérateurs.
A titre d'exemple, une scorie finale neutre ou légèrement basique sera utilisée pour fabriquer des liants hydrauliques de type pouzzolanique, tandis qu'une scorie basique et légèrement alumineuse entrera dans la fabrication de liants hydrauliques du type des
<Desc/Clms Page number 4>
ciments Portland. Une scorie basique et plus alumineuse permettra de fabriquer des poudres métallurgiques, destinées notamment à la désulfuration de l'acier.
Suivant une autre mise en oeuvre particulière, on laisse subsister, dans le four de fusion et/ou réduction, un talon de métal liquide à travers lequel on injecte les constituants traités ou les agents réactifs sous forme pulvérulente, afin de favoriser les réactions de réduction.
Après l'étape de réduction, on sépare le métal brut réduit, généralement riche en P et Mn, et une scorie contenant essentiellement CaO, MgO, AtOg, SiO.
Le métal ferreux réduit est ensuite soumis, à l'état liquide, à une étape de conditionnement, qui consiste essentiellement en une déphosphoration à l'aide d'une scorie appropriée.
Cette scorie de déphosphoration peut comprendre notamment des oxydes de fer Fie203, provenant par exemple de pailles de laminoirs. Elle peut encore avantageusement contenir un mélange d'oxydes CaO et Si02 en proportions appropriées, provenant par exemple d'une scorie peu phosphoreuse telle qu'une scorie LD ou une scorie de four électrique, ainsi qu'éventuellement un agent fondant tel que K2C03 par exemple.
Cette opération permet d'obtenir d'une part une fonte propre, directement utilisable au convertisseur ou au four électrique, et d'autre part une scorie phosphatée utilisable en agriculture.
En pratique, le procédé de l'invention permet de traiter en même temps des scories et des poussières, pour produire un métal propre utilisable dans une opération d'affinage conventionnel.
De plus, les scories produites par les deux étapes du procédé sont utilisables intégralement pour des applications classiques.
Ce procédé permet en outre d'obtenir un effet de masse, capable d'écrêter les variations de composition d'un bain d'acier et de diluer les parties minérales.
<Desc/Clms Page number 5>
Enfin, ce procédé ne génère pratiquement aucun résidu, ce qui est particulièrement intéressant pour la préservation de l'environnement.
<Desc / Clms Page number 1>
EMI1.1
Process for recovering iron-rich steel residues.
The present invention relates to a process for recovering iron-rich steel residues, such as slag and dust from steelworks and blast furnaces.
The various stages in the manufacture of a steel product are accompanied by the production of variable, sometimes significant, quantities of various residues. Many of these residues contain appreciable amounts of iron, usually in the form of oxides, which are lost to the current manufacturing process. These residues are, for example, dust and sludge from blast furnaces, slag, dust and sludge from steelworks, mill straws and pickling sludge.
There are currently many processes intended to recover one or the other type of residue, both inside and outside steel factories. For example, some steel slag is used in agriculture and some iron-rich dust is recycled in different forms in an electric steel furnace. However, recycling iron-rich dust is often complicated by the presence of zinc, in varying amounts, in this dust, in particular dust from blast furnaces.
It is common for recycling processes to generate residues which in turn must either be recycled, possibly outside the steel industry, or be landfilled, because there is no interesting outlet for them. .
The object of the present invention is to propose a process for recovering iron-rich steel residues, which aims to create, for the steel industry, a "zero waste" situation, in which any product obtained by steel operations can find a real use.
According to the present invention, a process for recovering iron-rich steel residues, is characterized in that a charge containing
<Desc / Clms Page number 2>
said residues, in that said molten charge is subjected to a step of reduction of at least a portion of the oxides which it contains to form a raw metal, and in that said raw metal is subjected to a step conditioning comprising a dephosphorization operation.
It goes without saying that the charge containing said residues can be initially, at least in part, in the molten state.
According to a particular implementation, the melting and the reduction of the charge can be carried out in a single step.
The charge is constituted by a mixture composed of iron-rich residues, such as those which have been mentioned above. Preferably, these residues comprise at least one steel slag.
Before and / or during the reduction step, a reducing agent is added to the charge, which is preferably a carbon compound.
If the melting and reduction are carried out in a single step, it is advantageous if the feed initially contains at least part of the required reducing agent.
In general, the mixture constituting the charge can be produced in any suitable manner, for example by placing the various constituents of the mixture separately in the melting or melting and reduction oven. It may however prove to be advantageous to produce this mixture outside the oven, so as to guarantee the precision of its composition as well as its homogeneity, and then to load it in the oven.
The residues constituting the feed may contain iron oxides, but also oxides or other compounds present in the steel slag. Likewise, dust incorporated into the mixture can introduce other metals into it, for example zinc or lead originating from blast furnace dust.
<Desc / Clms Page number 3>
The raw metal obtained from iron-rich residues of the aforementioned type is generally a pig iron, usable for the manufacture of carbon steel, mainly in an electric furnace.
According to an interesting variant, the residues comprise slag and / or dust rich in chromium and / or nickel. A load containing such residues will preferably be treated separately; the raw metal obtained under these conditions can in particular be used for the manufacture of ferro-alloys such as ferrochrome or ferronickel.
The reducing agent used is preferably a finely divided carbon agent, in particular pulverized coal; its combustion not only contributes to the heating and the melting of the charge, but also ensures the production of reducing gas, in particular CO, for the reduction of oxides.
The load can be heated by any suitable means, in particular by combustion of a combustible substance, electrically or by any combination of these two techniques. In addition to the melting of the charge and the production of reducing gas, it can also cause the vaporization of certain components such as lead or zinc introduced in particular by dust from blast furnaces; one can thus produce a highly concentrated zinc vapor, easily recoverable.
Finally, the charge can contain a mineral substance, known as a correction substance, the composition of which is chosen as a function of the composition of the starting mineral materials on the one hand and that of the desired final mineral phase on the other hand as a function of l intended use.
This mineral substance can in particular consist of oxidized compounds, such as silica or alumina, which are present in the slags of steelworks. Incinerator ash can also be used.
For example, a neutral or slightly basic final slag will be used to manufacture hydraulic binders of the pozzolanic type, while a basic and slightly aluminous slag will be used in the manufacture of hydraulic binders of the type
<Desc / Clms Page number 4>
Portland cements. A basic and more aluminous slag will make it possible to manufacture metallurgical powders, intended in particular for the desulfurization of steel.
According to another particular implementation, a heel of liquid metal is left in the melting and / or reduction furnace through which the treated constituents or the reactive agents are injected in powder form, in order to promote the reduction reactions. .
After the reduction step, the reduced crude metal, generally rich in P and Mn, is separated from a slag essentially containing CaO, MgO, AtOg, SiO.
The reduced ferrous metal is then subjected, in the liquid state, to a conditioning step, which essentially consists of dephosphorization using an appropriate slag.
This dephosphorization slag may in particular comprise iron oxides Fie203, originating for example from rolling mill straws. It may also advantageously contain a mixture of CaO and SiO2 oxides in appropriate proportions, for example from a low phosphorous slag such as an LD slag or an electric furnace slag, as well as possibly a fluxing agent such as K2C03 by example.
This operation makes it possible on the one hand to obtain a clean cast iron, which can be used directly in a converter or in an electric oven, and on the other hand a phosphate slag which can be used in agriculture.
In practice, the method of the invention makes it possible to treat slag and dust at the same time, to produce a clean metal which can be used in a conventional refining operation.
In addition, the slag produced by the two stages of the process can be fully used for conventional applications.
This process also makes it possible to obtain a mass effect, capable of clipping the variations in composition of a steel bath and of diluting the mineral parts.
<Desc / Clms Page number 5>
Finally, this process generates practically no residue, which is particularly advantageous for the preservation of the environment.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| BE9500623A BE1009828A3 (en) | 1995-07-13 | 1995-07-13 | Method of recovering iron-rich iron and steel manufacturing residues |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| BE9500623A BE1009828A3 (en) | 1995-07-13 | 1995-07-13 | Method of recovering iron-rich iron and steel manufacturing residues |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| BE1009828A3 true BE1009828A3 (en) | 1997-10-07 |
Family
ID=3889099
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| BE9500623A BE1009828A3 (en) | 1995-07-13 | 1995-07-13 | Method of recovering iron-rich iron and steel manufacturing residues |
Country Status (1)
| Country | Link |
|---|---|
| BE (1) | BE1009828A3 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115029498A (en) * | 2022-06-28 | 2022-09-09 | 广东韶钢松山股份有限公司 | Method for smelting blast furnace residual iron by converter |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB408254A (en) * | 1931-08-31 | 1934-03-29 | Electro Chimie Metal | Process for dephosphorising steel |
| GB2054657A (en) * | 1979-05-30 | 1981-02-18 | Arbed | Process and installation for the treatment of dust and sludge from blast furnaces, and electric furnaces and converters of steel works |
| JPS6029409A (en) * | 1983-07-27 | 1985-02-14 | Sumitomo Metal Ind Ltd | Method for decarburizing and dephosphorizing molten steel |
| JPS60218415A (en) * | 1984-04-12 | 1985-11-01 | Nippon Jiryoku Senko Kk | Treatment of steel making dust, sludge or the like |
| WO1991012210A1 (en) * | 1990-02-13 | 1991-08-22 | The Illawarra Technology Corporation Ltd. | Cotreatment of sewage and steelworks wastes |
| DE4123626A1 (en) * | 1991-07-17 | 1993-01-21 | Intercept Ag | Reconditioning metallurgical residues with reduced installation costs - involves agglomeration or pelleting of residues, supplying to counted-flow melting unit with dust filter, heating and drying, etc. |
| EP0657549A1 (en) * | 1993-12-10 | 1995-06-14 | Voest-Alpine Industrieanlagenbau Gmbh | Process for producing an iron melt |
-
1995
- 1995-07-13 BE BE9500623A patent/BE1009828A3/en not_active IP Right Cessation
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB408254A (en) * | 1931-08-31 | 1934-03-29 | Electro Chimie Metal | Process for dephosphorising steel |
| GB2054657A (en) * | 1979-05-30 | 1981-02-18 | Arbed | Process and installation for the treatment of dust and sludge from blast furnaces, and electric furnaces and converters of steel works |
| JPS6029409A (en) * | 1983-07-27 | 1985-02-14 | Sumitomo Metal Ind Ltd | Method for decarburizing and dephosphorizing molten steel |
| JPS60218415A (en) * | 1984-04-12 | 1985-11-01 | Nippon Jiryoku Senko Kk | Treatment of steel making dust, sludge or the like |
| WO1991012210A1 (en) * | 1990-02-13 | 1991-08-22 | The Illawarra Technology Corporation Ltd. | Cotreatment of sewage and steelworks wastes |
| DE4123626A1 (en) * | 1991-07-17 | 1993-01-21 | Intercept Ag | Reconditioning metallurgical residues with reduced installation costs - involves agglomeration or pelleting of residues, supplying to counted-flow melting unit with dust filter, heating and drying, etc. |
| EP0657549A1 (en) * | 1993-12-10 | 1995-06-14 | Voest-Alpine Industrieanlagenbau Gmbh | Process for producing an iron melt |
Non-Patent Citations (3)
| Title |
|---|
| "recycling stainless steelmaking dust using a DC arc furnace", STEEL TIMES, vol. 221, no. 11, November 1993 (1993-11-01), REDHILL, GB, pages 481 - 482, XP000420664 * |
| PATENT ABSTRACTS OF JAPAN vol. 10, no. 85 (C - 336)<2142> 4 April 1986 (1986-04-04) * |
| PATENT ABSTRACTS OF JAPAN vol. 9, no. 145 (C - 287) 20 June 1985 (1985-06-20) * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115029498A (en) * | 2022-06-28 | 2022-09-09 | 广东韶钢松山股份有限公司 | Method for smelting blast furnace residual iron by converter |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP2383352B1 (en) | Method for reclaiming iron and phosphorus from steelmaking slag | |
| US20080156144A1 (en) | Method for reducing to metallic chromium the chromium oxide in slag from stainless steel processing | |
| AU2652201A (en) | Method for treating slags or slag mixtures on an iron bath | |
| BE1009828A3 (en) | Method of recovering iron-rich iron and steel manufacturing residues | |
| US4795491A (en) | Premelted synthetic slag for ladle desulfurizing molten steel | |
| KR20220098213A (en) | Molten Steel Manufacturing Method | |
| US4853034A (en) | Method of ladle desulfurizing molten steel | |
| HU187645B (en) | Process for the production of complex ferro-alloys of si-base | |
| CA1174855A (en) | Method of producing molten metal consisting mainly of manganese and iron | |
| RU2201970C2 (en) | Method of making steel in high-power electric arc furnaces | |
| EP0605378A1 (en) | Method of valorizing the slag of a steelmaking electric furnace | |
| JPH0437136B2 (en) | ||
| JP3158912B2 (en) | Stainless steel refining method | |
| US6059854A (en) | Process for processing waste incineration residues | |
| FI69647B (en) | FOERFARANDE FOER FRAMSTAELLNING OCH BEHANDLING AV FERROKROM | |
| RU2091494C1 (en) | Method of smelting steel alloyed with chromium and nickel | |
| SK283194B6 (en) | Method of producing pig iron, alloys of ferrous metal and/ or non-ferrous metal with synthetic blast furnace slag from residues of incinerated waste and steelworks slag | |
| US3834899A (en) | Method of manufacturing low-carbon ferrochromium | |
| RU2805114C1 (en) | Steel melting method in electric arc furnace | |
| ZA200206543B (en) | Method relating to manufacturing of steel. | |
| SU1388437A1 (en) | Slag-formingg mixture | |
| EP0024065A1 (en) | Processes for working-up non-phosphorous metallurgical slags | |
| Amelin et al. | Technology for the reduction of iron oxides in the processing of metal slag scrap in the oxygen converter | |
| SU572504A1 (en) | Method for maunfacturing iron and its alloys from iron ore | |
| KR101550999B1 (en) | Steelmaking refining method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| RE | Patent lapsed |
Effective date: 20100731 |