US3376130A - Process for dephosphorization of pig iron particularly pig iron rich in phosphorus - Google Patents
Process for dephosphorization of pig iron particularly pig iron rich in phosphorus Download PDFInfo
- Publication number
- US3376130A US3376130A US43666165A US3376130A US 3376130 A US3376130 A US 3376130A US 43666165 A US43666165 A US 43666165A US 3376130 A US3376130 A US 3376130A
- Authority
- US
- United States
- Prior art keywords
- slag
- bath
- phosphorus
- pig iron
- iron
- 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.)
- Expired - Lifetime
Links
- 229910052698 phosphorus Inorganic materials 0.000 title claims description 30
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 title claims description 25
- 229910000805 Pig iron Inorganic materials 0.000 title claims description 25
- 238000000034 method Methods 0.000 title claims description 25
- 239000011574 phosphorus Substances 0.000 title claims description 25
- 239000002893 slag Substances 0.000 claims description 50
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 24
- 239000000463 material Substances 0.000 claims description 13
- 229910052742 iron Inorganic materials 0.000 claims description 12
- 229910052760 oxygen Inorganic materials 0.000 claims description 12
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 11
- 238000007664 blowing Methods 0.000 claims description 11
- 239000001301 oxygen Substances 0.000 claims description 11
- 239000002253 acid Substances 0.000 claims description 10
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 10
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 8
- DLYUQMMRRRQYAE-UHFFFAOYSA-N tetraphosphorus decaoxide Chemical compound O1P(O2)(=O)OP3(=O)OP1(=O)OP2(=O)O3 DLYUQMMRRRQYAE-UHFFFAOYSA-N 0.000 claims description 8
- 239000000292 calcium oxide Substances 0.000 claims description 6
- 239000000155 melt Substances 0.000 claims description 6
- 230000002378 acidificating effect Effects 0.000 claims description 5
- 239000003337 fertilizer Substances 0.000 claims description 5
- 239000000395 magnesium oxide Substances 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 4
- 229910000272 alkali metal oxide Inorganic materials 0.000 claims description 3
- 239000002826 coolant Substances 0.000 claims description 3
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims description 2
- 230000003993 interaction Effects 0.000 claims description 2
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 claims description 2
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims description 2
- 239000000377 silicon dioxide Substances 0.000 claims description 2
- 235000012239 silicon dioxide Nutrition 0.000 claims description 2
- 239000004408 titanium dioxide Substances 0.000 claims description 2
- 238000007670 refining Methods 0.000 description 21
- 229910052799 carbon Inorganic materials 0.000 description 13
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 12
- 235000011941 Tilia x europaea Nutrition 0.000 description 12
- 239000004571 lime Substances 0.000 description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 10
- 238000007792 addition Methods 0.000 description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 229910000831 Steel Inorganic materials 0.000 description 6
- 239000010959 steel Substances 0.000 description 6
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 5
- 235000012255 calcium oxide Nutrition 0.000 description 5
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 239000005864 Sulphur Substances 0.000 description 4
- 238000005261 decarburization Methods 0.000 description 4
- 238000005187 foaming Methods 0.000 description 4
- 229910052748 manganese Inorganic materials 0.000 description 4
- 239000011572 manganese Substances 0.000 description 4
- 150000007513 acids Chemical class 0.000 description 3
- 239000002585 base Substances 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 238000005262 decarbonization Methods 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 230000003292 diminished effect Effects 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 235000013980 iron oxide Nutrition 0.000 description 1
- VBMVTYDPPZVILR-UHFFFAOYSA-N iron(2+);oxygen(2-) Chemical class [O-2].[Fe+2] VBMVTYDPPZVILR-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 230000001020 rhythmical effect Effects 0.000 description 1
- 150000003388 sodium compounds Chemical class 0.000 description 1
- 238000003756 stirring Methods 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
- 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
- C21C5/28—Manufacture of steel in the converter
- C21C5/30—Regulating or controlling the blowing
- C21C5/32—Blowing from above
-
- 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
Definitions
- Steps used in these processes comprise maintaining a high basic slag, the addition of ores or slag fluxing means, limiting the temperature, control of the blast jet to a low velocity against the bath surface, providing an additional mechanical movement to the bath, addition of pulverized lime to the oxygen blast jet and others.
- the refining of high phosphorus pig iron is carried out in a vessel which is stationary during the refining with oxygen being blown perpendicularly onto the bath surface and the oxygen usually contains ground lime.
- a first phosphate slag is withdrawn when the percentage of carbon has been reduced to about 1%, at which time the percentage of phosphorus in the steels is in the range of 0.2%-O.3%.
- the temperature must be far above 1500 C., as, for example, about 1600 C., in order to liquidize the highly basic slag.
- These slags have a ratio of basicity, i.e., bases to acids, of at least 2.
- the final slags which are preferably left in the refining vessel, are still more basic and usually have a ratio of basicity of 3 or more and their ferrous oxide content are high.
- the decarburization reaction not only has to deliver the necessary heat, but in addition imparts a movement to the bath during decarburization by the gas evolved and thereby produces a thorough circulation.
- the stirring exect of the decarburization reaction may not be necessary in principle to produce the dephosphorization reaction, in such methods where mechanical movement is imparted to the bath, as in a Kaldo furnace, it is always used.
- Acid slag materials most suitable are SiO P 0 TiO A1 0
- the process is particularly adapted for the refining of high phosphorus pig iron (above 1.5% P), such as pig iron for basic Bessemer. Furthermore it is necessary with this method to keep the temperature low, namely below 1500 C., preferably within the limits 1400 C. and 1450 C. This is not only because the dephosphorization will proceed better at so low a temperature, but also because at temperatures above 1500 C. such low basicity slags cannot be used in basic vessels as they tend to attack the lining and dissolve CaO and MgO therefrom.
- This mechanical movement of the bath can be produced by impressing a rotary swinging movement upon the bath while contained in a vertical converter vessel, such as that resulting from an eccentric movement of the vessel about a vertical axis without rotation of the vessel about said axis.
- Such a movement to the bath can also be produced by other rhythmic movement of the converter vessel in resonance with the swinging movement of the bath.
- the process according to the invention also can be carried out in refining vessels classified as rotary either about a horizontal or inclined axis during the refining.
- the required maximum temperature limit is maintained by adding cooling agents, such as scrap iron, before or during the refining.
- the slag was maintained substantially constant during the entire course of blowing at 37%-39% CaO, 1%1.5% MgO, 6%-8% SiO 25%29% P 0 1%-2% A1 0 12%15% MnO, 8%-10% FeO.
- the slag had low viscosity, and had a fine foam when the furnace was tilted, which collapsed quickly, did not retain any granules and could easily be removed.
- a further surprising feature of this process was that the sulphur in the pig iron also was reduced by 50-60%, for instance, from 0.040% in the pig iron to 0.015- 0.020%, although slags which are acid from a metallurgical point of view do not take up very much sulphur. Also the content of nitrogen had decreased to below 0.002%.
- the slag can be removed and a high percentage of very easily soluble phosphoric acid can be recovered which is a highly elfective fertilizer.
- the pig iron is then decarburized in the usual way after repeated small additions of lime, preferably not more than 35 kg. lime per ton pig iron, until desired end percentage of carbon is attained. During this finishing refining the phosphorus percentage decreases to below 0.020%, the percentage of sulphur to about 0.010%, the percentage of nitrogen remaining unchanged below 0.002%, or decreasing further somewhat during the decarburization. It is cooled as required. The end slag obtained is preferably left in the converter for a subsequent heat.
- a process for dephosphorizing a bath of moltenhigh phosphorus pig iron and producing slag having a high phosphorus content for use as a fertilizer comprising the steps of blowing oxygen onto the bath and a layer of slag floating on the top thereof, adding basic slag-forming material selected from the group consisting of calcium oxide, magnesium oxide, alkali metal oxide and mixtures thereof and acid slag forming material selected from the group consisting of silicon dioxide, titanium dioxide, aluminum oxide, phosphorus pentoxide and mixtures thereof, the proportions of said basic and acidic slag-forming materials being such during the entire blowing period as to maintain a ratio of basic to acidic materials in the slag in the range of 0.8 to 1.5 by weight, maintaining the bath at a temperature below 1500 C.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Carbon Steel Or Casting Steel Manufacturing (AREA)
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE1964T0025740 DE1433649A1 (de) | 1964-03-03 | 1964-03-03 | Verfahren zum Entphosphoren von Roheisen,insbesondere Thomasroheisen |
Publications (1)
Publication Number | Publication Date |
---|---|
US3376130A true US3376130A (en) | 1968-04-02 |
Family
ID=7552277
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US43666165 Expired - Lifetime US3376130A (en) | 1964-03-03 | 1965-03-02 | Process for dephosphorization of pig iron particularly pig iron rich in phosphorus |
Country Status (6)
Country | Link |
---|---|
US (1) | US3376130A (da) |
BE (1) | BE660381A (da) |
DE (1) | DE1433649A1 (da) |
FR (1) | FR1425195A (da) |
GB (1) | GB1097512A (da) |
LU (1) | LU48051A1 (da) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3473917A (en) * | 1966-08-25 | 1969-10-21 | Bot Brassert Oxygen Technik Ag | Basic steelmaking process |
EP0043238A1 (en) * | 1980-06-28 | 1982-01-06 | Kawasaki Steel Corporation | Method of dephosphorizing molten pig iron |
EP0170407A1 (en) * | 1984-06-27 | 1986-02-05 | The BOC Group, Inc. | Agents for the removal of impurities from a molten metal and a process for producing same |
JP2013181215A (ja) * | 2012-03-01 | 2013-09-12 | Jfe Steel Corp | 溶銑吹錬処理の制御方法および制御装置 |
JP2013181216A (ja) * | 2012-03-01 | 2013-09-12 | Jfe Steel Corp | 溶銑吹錬処理の制御方法および制御装置 |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2391280A2 (fr) * | 1977-05-17 | 1978-12-15 | Sumitomo Metal Ind | Procede de dephosphoration de la fonte liquide |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2668759A (en) * | 1952-05-22 | 1954-02-09 | Inland Steel Co | Steelmaking process |
US2671018A (en) * | 1952-03-31 | 1954-03-02 | Huettenwerk Oberhausen Ag | Process for the production of basic bessemer steel low in nitrogen |
US2693411A (en) * | 1951-12-26 | 1954-11-02 | Cremer Frederick | Method of purifying molten pig iron |
US2781256A (en) * | 1953-11-23 | 1957-02-12 | United States Steel Corp | Process for the rapid removal of sulphur and silicon from pig iron |
US2789046A (en) * | 1955-02-01 | 1957-04-16 | Mannesmann Ag | Process of making steel from pig iron |
GB817786A (en) * | 1956-08-16 | 1959-08-06 | Stora Kopparbergs Bergslags Ab | Method of refining phosphorus-containing pig iron |
GB946964A (en) * | 1960-12-22 | 1964-01-15 | Halbergerhuette Ges Mit Beschr | Dephosphorization of melts of ferrous metals |
US3136626A (en) * | 1960-08-19 | 1964-06-09 | Lorraine Laminage | Method of refining cast-iron |
US3172756A (en) * | 1965-03-09 | Process of dephosphorizing pig iron |
-
1964
- 1964-03-03 DE DE1964T0025740 patent/DE1433649A1/de active Pending
-
1965
- 1965-02-10 GB GB582465A patent/GB1097512A/en not_active Expired
- 1965-02-23 LU LU48051A patent/LU48051A1/xx unknown
- 1965-02-24 FR FR6870A patent/FR1425195A/fr not_active Expired
- 1965-02-26 BE BE660381D patent/BE660381A/xx unknown
- 1965-03-02 US US43666165 patent/US3376130A/en not_active Expired - Lifetime
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3172756A (en) * | 1965-03-09 | Process of dephosphorizing pig iron | ||
US2693411A (en) * | 1951-12-26 | 1954-11-02 | Cremer Frederick | Method of purifying molten pig iron |
US2671018A (en) * | 1952-03-31 | 1954-03-02 | Huettenwerk Oberhausen Ag | Process for the production of basic bessemer steel low in nitrogen |
US2668759A (en) * | 1952-05-22 | 1954-02-09 | Inland Steel Co | Steelmaking process |
US2781256A (en) * | 1953-11-23 | 1957-02-12 | United States Steel Corp | Process for the rapid removal of sulphur and silicon from pig iron |
US2789046A (en) * | 1955-02-01 | 1957-04-16 | Mannesmann Ag | Process of making steel from pig iron |
GB817786A (en) * | 1956-08-16 | 1959-08-06 | Stora Kopparbergs Bergslags Ab | Method of refining phosphorus-containing pig iron |
US3136626A (en) * | 1960-08-19 | 1964-06-09 | Lorraine Laminage | Method of refining cast-iron |
GB946964A (en) * | 1960-12-22 | 1964-01-15 | Halbergerhuette Ges Mit Beschr | Dephosphorization of melts of ferrous metals |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3473917A (en) * | 1966-08-25 | 1969-10-21 | Bot Brassert Oxygen Technik Ag | Basic steelmaking process |
EP0043238A1 (en) * | 1980-06-28 | 1982-01-06 | Kawasaki Steel Corporation | Method of dephosphorizing molten pig iron |
EP0170407A1 (en) * | 1984-06-27 | 1986-02-05 | The BOC Group, Inc. | Agents for the removal of impurities from a molten metal and a process for producing same |
JP2013181215A (ja) * | 2012-03-01 | 2013-09-12 | Jfe Steel Corp | 溶銑吹錬処理の制御方法および制御装置 |
JP2013181216A (ja) * | 2012-03-01 | 2013-09-12 | Jfe Steel Corp | 溶銑吹錬処理の制御方法および制御装置 |
Also Published As
Publication number | Publication date |
---|---|
LU48051A1 (da) | 1965-04-23 |
DE1433649A1 (de) | 1969-05-14 |
GB1097512A (en) | 1968-01-03 |
BE660381A (da) | 1965-08-26 |
FR1425195A (fr) | 1966-01-14 |
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