EP0064019A1 - Procédé et installation de désulfuration de fer fondu - Google Patents
Procédé et installation de désulfuration de fer fondu Download PDFInfo
- Publication number
- EP0064019A1 EP0064019A1 EP82630024A EP82630024A EP0064019A1 EP 0064019 A1 EP0064019 A1 EP 0064019A1 EP 82630024 A EP82630024 A EP 82630024A EP 82630024 A EP82630024 A EP 82630024A EP 0064019 A1 EP0064019 A1 EP 0064019A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- melt
- solids
- gases
- gas
- lime
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
- 239000000155 melt Substances 0.000 title claims abstract description 33
- 238000000034 method Methods 0.000 title claims abstract description 32
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims description 12
- 229910052742 iron Inorganic materials 0.000 title claims description 6
- 239000007789 gas Substances 0.000 claims abstract description 28
- 239000007787 solid Substances 0.000 claims abstract description 22
- 239000000203 mixture Substances 0.000 claims abstract description 20
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims abstract description 15
- 235000011941 Tilia x europaea Nutrition 0.000 claims abstract description 15
- 239000004571 lime Substances 0.000 claims abstract description 15
- 239000012159 carrier gas Substances 0.000 claims abstract description 14
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000001301 oxygen Substances 0.000 claims abstract description 6
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 6
- 229910001338 liquidmetal Inorganic materials 0.000 claims abstract description 5
- 230000007935 neutral effect Effects 0.000 claims abstract description 5
- 239000004575 stone Substances 0.000 claims abstract description 5
- 230000001681 protective effect Effects 0.000 claims abstract description 4
- 229910052751 metal Inorganic materials 0.000 claims description 6
- 239000002184 metal Substances 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 5
- 230000001413 cellular effect Effects 0.000 claims description 4
- 239000000161 steel melt Substances 0.000 claims description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- 230000003009 desulfurizing effect Effects 0.000 claims description 2
- 239000004570 mortar (masonry) Substances 0.000 claims description 2
- 230000009257 reactivity Effects 0.000 claims description 2
- 230000004907 flux Effects 0.000 abstract description 2
- 239000002893 slag Substances 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 238000007664 blowing Methods 0.000 description 6
- 239000011575 calcium Substances 0.000 description 6
- 238000006477 desulfuration reaction Methods 0.000 description 6
- 230000023556 desulfurization Effects 0.000 description 6
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical class [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 5
- 229910052791 calcium Inorganic materials 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 238000007654 immersion Methods 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 229940043430 calcium compound Drugs 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 229910014813 CaC2 Inorganic materials 0.000 description 1
- 229910004709 CaSi Inorganic materials 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 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
- 150000001674 calcium compounds Chemical class 0.000 description 1
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical compound [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 description 1
- 229910001634 calcium fluoride Inorganic materials 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 239000010459 dolomite Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 230000009970 fire resistant effect Effects 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- 235000014380 magnesium carbonate Nutrition 0.000 description 1
- 239000001095 magnesium carbonate Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000010310 metallurgical process Methods 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000010405 reoxidation reaction Methods 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
Classifications
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D1/00—Treatment of fused masses in the ladle or the supply runners before casting
- B22D1/002—Treatment with gases
- B22D1/005—Injection assemblies therefor
Definitions
- the present invention relates to a process for the desulfurization of molten iron, in particular molten steel, and the device required for this.
- Calcium or calcium compounds such as CaO, CaF2, CaSi, CaC2, are mainly suitable as desulfurizing agents; the carrier gas is a neutral gas, e.g. Argon.
- the slag should have less than 2% FeO, the mouth of the injection lance should be lower than 2000 mm below the bath level and the deoxidation should have been carried out in such a way that there is more than 0.015% Al in the metal phase.
- the immersion depth ⁇ of the blowing lance should be at least 2 m; in the specific exemplary embodiment, 2.6 m are specified for a 4 m high pan.
- calcium is assumed to have a vapor pressure of 2.13 atm at 1600 ° C. has liquid in the melt, provided it is at least 1.7 m below the bath surface. It is taught, for example, that the liquid calcium drops rise much more slowly than the vapor bubbles, which results in an extended reaction time and thus a better use of the calcium quantities used.
- the aim of the present invention was to propose a method which largely dispenses with the use of strongly cooling aids, which avoids the time-consuming and temperature-sensitive transferring and which does not require the use of expensive and wear-resistant blowing lances and, moreover, through long-term contact between the melt and the Treatment substances prolonged reaction times as well as an improved utilization of the reagents.
- This goal is achieved by the process according to the invention, which provides for largely removing the steel melt immediately after it has been refreshed, and then supplying it with gases and solids suspended in gases individually and in combination as required, using one and the same feed unit from below, the latter essentially consisting of one there is a refractory vessel bottom stone which is provided with oriented passages of such a type that they are gas-permeable at the same time without allowing the passage of liquid metal and switching on both the gas supply and the solids supply as required, and to control and interrupt them in terms of quantity.
- the first process step according to the invention is to remove the melt as completely as possible. This step is essential since, as is well known, in the absence of furnace slag, the tendency to absorb nitrogen and hydrogen in the melt is markedly suppressed.
- the covering of the bath with pure lime according to the invention mentioned later, is to be seen primarily as a protective measure against nitrogen or hydrogen uptake and only secondarily as a hate measure to influence the metallurgical processes at the phase boundaries. In fact, it was found that both nitrogen and hydrogen penetrate into the metal matrix during the subsequent desulfurization, provided that furnace slag of a certain composition is sufficient the quantities are available.
- the next step consists in introducing pure lime into the melt with the aid of a neutral carrier gas through the charging unit, which is arranged in groups in the bottom of the metallurgical vessel.
- a neutral carrier gas for example, serves as the carrier gas. This measure serves to cover the melt and thus to protect against the absorption of unwanted gases from the air.
- a further protective measure against the uptake of N2 or H2 is carried out by closing the vessel with a tightly fitting lid, which only has openings for inserting measuring probes to record the temperature and possibly the oxygen activity.
- the lime supply is throttled and metallic aluminum is mixed in with the aid of which the melt is deoxidized.
- the aluminum powder introduced from below deoxidizes the melt particularly effectively; It is important to use aluminum in a mixture with lime in a ratio of 1: 1 to 1: 5 for the smooth passage of the aluminum through the charging unit.
- melt is deoxidized to a maximum of 35 ppm 02, then a mixture consisting of metallic aluminum at 0-30% by weight, from flux paste at 0-20% by weight and from lime at 50-100 is always passed through the same charging unit % By weight in the melt.
- the blowing process itself, it must be said that it takes place according to the invention by setting a constant carrier gas flow through the charging unit and varying the amount of mixture to be introduced per unit of time, as required. Depending on the melting temperature, the amount of mixture will be kept constant over the treatment period, or the main proportion will be entered within the initial period. Alternatively, it is provided according to the invention that the amount of mixture per unit of time is kept constant and the carrier gas flow is varied, in particular if, at certain points in time, greater or weaker whirling of the bath is important.
- the Flexibility of the method according to the invention allows the solids supply to be throttled, interrupted and switched on again after sufficient swirling in the bath.
- Each loading unit understands a refractory, gas-permeable structure, which consists of at least two fire-resistant, unfired, e.g. with a carbon carrier bound or chemically bound material existing segments are built, which are provided on at least one longitudinal surface with a wear-resistant pad.
- the segments are combined by a common metal housing, which lies tightly against the longitudinal surfaces of the segments, possibly with the interposition of a mortar layer, with at least one connection and a distribution space for the material supply being arranged on an end face of the structure and the connection with at least one gas and is connected to at least one solid material feed device, each of which understands a metering device.
- gas-permeable structures which are provided in accordance with the prior art for supplying gases into liquid metals and as described by the applicant in her Germany patents LU 82.552, 82.553, 82.554, 82.597 are used for the combined introduction of gases and solids, what by coupling the structure with also known, but in others Connections used solid feed devices is enabled.
- the dosing device for solids is usefully a per se known cellular wheel blow-through lock as the applicant has described it eg in its Luxembourg patent LU 80.692.
- the latter enables a stepless variation of the amount of mixture to be entered per unit of time, which can only be brought about by changing the cellular wheel rotation speed, the carrier gas flow rate being able to be varied independently of this.
- a particularly favorable procedure is also made possible by the fact that the amount of desulphurization agents actually blown in can be determined continuously, and it is sufficient to do this by continuously measuring the weight of the emptying mixture storage container; a measure that does not allow the construction of most conventional systems.
- melts desulphurized by the process according to the invention not only have the desired low sulfur content, but the metal itself is characterized by an extremely low content of inclusions, the latter being extremely spherical in character.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Treatment Of Steel In Its Molten State (AREA)
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| LU83314A LU83314A1 (de) | 1981-04-24 | 1981-04-24 | Verfahren und vorrichtung zum entschwefeln von eisenschmelzen |
| LU83314 | 1981-04-24 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| EP0064019A1 true EP0064019A1 (fr) | 1982-11-03 |
Family
ID=19729633
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP82630024A Withdrawn EP0064019A1 (fr) | 1981-04-24 | 1982-03-24 | Procédé et installation de désulfuration de fer fondu |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US4415358A (fr) |
| EP (1) | EP0064019A1 (fr) |
| JP (1) | JPS57181321A (fr) |
| LU (1) | LU83314A1 (fr) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0263255A1 (fr) * | 1986-08-11 | 1988-04-13 | Arbed S.A. | Procédé et agent pour chauffer et purifier simultanément des bains métalliques |
| DE4003879C1 (fr) * | 1990-02-08 | 1991-07-18 | China Steel Corp., Kaohsiung City, Hsiao-Kang, Tw |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2256427B (en) * | 1991-06-01 | 1994-05-11 | B & K Engineering Co | Flux injecting machines |
| US5324341A (en) * | 1992-05-05 | 1994-06-28 | Molten Metal Technology, Inc. | Method for chemically reducing metals in waste compositions |
| LU92813B1 (en) * | 2015-09-02 | 2017-03-20 | Wurth Paul Sa | Enhanced pressurising of bulk material in lock hoppers |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE928955C (de) * | 1952-08-17 | 1955-06-16 | Huettenwerk Haspe Ag | Verfahren zum Entschwefeln von Roheisen |
| DE1583219A1 (de) * | 1967-11-28 | 1970-07-30 | Basf Ag | Verfahren zur Behandlung von Metallschmelzen,vorzugsweise von Stahlschmelzen |
| DE2209902B2 (de) * | 1972-03-01 | 1975-01-16 | Thyssen Niederrhein Ag Huetten- Und Walzwerke, 4200 Oberhausen | Verfahren zur Entschwefelung von Stahlschmelzen |
| DE2559188A1 (de) * | 1975-01-14 | 1976-07-15 | Inteco Int Techn Beratung | Verfahren zur entschwefelung von stahlschmelzen |
| DE2602536A1 (de) * | 1975-01-23 | 1976-07-29 | Uss Eng & Consult | Verfahren zur herstellung von schwefelarmen blasstahl |
| EP0013550A1 (fr) * | 1978-12-21 | 1980-07-23 | Arbed S.A. | Procédé et installation de désulfuration de fer fondu |
| EP0021861A1 (fr) * | 1979-04-25 | 1981-01-07 | INSTITUT DE RECHERCHES DE LA SIDERURGIE FRANCAISE (IRSID) France | Pièce réfractaire perméable aux gaz et son procédé de fabrication |
| EP0043338A1 (fr) * | 1980-06-25 | 1982-01-06 | Arbed S.A. | Elément réfractaire perméable aux gaz |
| EP0043787A1 (fr) * | 1980-07-09 | 1982-01-13 | Arbed S.A. | Elément réfractaire perméable aux gaz |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR90350E (fr) * | 1965-10-21 | 1967-11-24 | Air Liquide | Procédé de traitement des métaux liquides, applicable notamment à l'élaboration de fonte nodulaire |
| US3574596A (en) * | 1967-09-15 | 1971-04-13 | Amsted Ind Inc | Method for producing stainless steel |
| US3598383A (en) * | 1969-01-14 | 1971-08-10 | William H Moore | Method and apparatus for incorporating additives in a melt |
| US3610602A (en) * | 1969-10-14 | 1971-10-05 | United States Steel Corp | Gas-permeable refractory plug and method |
-
1981
- 1981-04-24 LU LU83314A patent/LU83314A1/de unknown
-
1982
- 1982-03-24 EP EP82630024A patent/EP0064019A1/fr not_active Withdrawn
- 1982-04-23 US US06/371,439 patent/US4415358A/en not_active Expired - Fee Related
- 1982-04-23 JP JP57067530A patent/JPS57181321A/ja active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE928955C (de) * | 1952-08-17 | 1955-06-16 | Huettenwerk Haspe Ag | Verfahren zum Entschwefeln von Roheisen |
| DE1583219A1 (de) * | 1967-11-28 | 1970-07-30 | Basf Ag | Verfahren zur Behandlung von Metallschmelzen,vorzugsweise von Stahlschmelzen |
| DE2209902B2 (de) * | 1972-03-01 | 1975-01-16 | Thyssen Niederrhein Ag Huetten- Und Walzwerke, 4200 Oberhausen | Verfahren zur Entschwefelung von Stahlschmelzen |
| DE2559188A1 (de) * | 1975-01-14 | 1976-07-15 | Inteco Int Techn Beratung | Verfahren zur entschwefelung von stahlschmelzen |
| DE2602536A1 (de) * | 1975-01-23 | 1976-07-29 | Uss Eng & Consult | Verfahren zur herstellung von schwefelarmen blasstahl |
| EP0013550A1 (fr) * | 1978-12-21 | 1980-07-23 | Arbed S.A. | Procédé et installation de désulfuration de fer fondu |
| EP0021861A1 (fr) * | 1979-04-25 | 1981-01-07 | INSTITUT DE RECHERCHES DE LA SIDERURGIE FRANCAISE (IRSID) France | Pièce réfractaire perméable aux gaz et son procédé de fabrication |
| EP0043338A1 (fr) * | 1980-06-25 | 1982-01-06 | Arbed S.A. | Elément réfractaire perméable aux gaz |
| EP0043787A1 (fr) * | 1980-07-09 | 1982-01-13 | Arbed S.A. | Elément réfractaire perméable aux gaz |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0263255A1 (fr) * | 1986-08-11 | 1988-04-13 | Arbed S.A. | Procédé et agent pour chauffer et purifier simultanément des bains métalliques |
| DE4003879C1 (fr) * | 1990-02-08 | 1991-07-18 | China Steel Corp., Kaohsiung City, Hsiao-Kang, Tw |
Also Published As
| Publication number | Publication date |
|---|---|
| US4415358A (en) | 1983-11-15 |
| LU83314A1 (de) | 1983-03-24 |
| JPS57181321A (en) | 1982-11-08 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
| AK | Designated contracting states |
Designated state(s): AT BE DE FR GB IT NL SE |
|
| 17P | Request for examination filed |
Effective date: 19830425 |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
|
| 18D | Application deemed to be withdrawn |
Effective date: 19841016 |
|
| RIN1 | Information on inventor provided before grant (corrected) |
Inventor name: SCHLEIMER, FRANCOIS Inventor name: GOEDERT, JEAN Inventor name: WEINER, ANTOINE Inventor name: LEGILLE, EDOUARD Inventor name: METZ, PAUL |