US3856510A - Pig iron refining process - Google Patents
Pig iron refining process Download PDFInfo
- Publication number
- US3856510A US3856510A US00347521A US34752173A US3856510A US 3856510 A US3856510 A US 3856510A US 00347521 A US00347521 A US 00347521A US 34752173 A US34752173 A US 34752173A US 3856510 A US3856510 A US 3856510A
- Authority
- US
- United States
- Prior art keywords
- blowing
- converter
- tuyere
- oxidizing gas
- protective fluid
- 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
- 229910000805 Pig iron Inorganic materials 0.000 title claims abstract description 21
- 238000000034 method Methods 0.000 title claims description 26
- 238000007670 refining Methods 0.000 title claims description 18
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 21
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 21
- 239000001301 oxygen Substances 0.000 claims abstract description 21
- 239000012530 fluid Substances 0.000 claims abstract description 20
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 19
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims abstract description 18
- 230000001681 protective effect Effects 0.000 claims abstract description 16
- 229910052751 metal Inorganic materials 0.000 claims abstract description 14
- 239000002184 metal Substances 0.000 claims abstract description 14
- 239000000155 melt Substances 0.000 claims abstract description 13
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000001294 propane Substances 0.000 claims abstract description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 27
- 238000007664 blowing Methods 0.000 claims description 21
- 239000007789 gas Substances 0.000 claims description 15
- 229910052742 iron Inorganic materials 0.000 claims description 14
- 230000001590 oxidative effect Effects 0.000 claims description 14
- 239000002893 slag Substances 0.000 claims description 13
- 229910052698 phosphorus Inorganic materials 0.000 claims description 12
- 230000002093 peripheral effect Effects 0.000 claims description 9
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 5
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 5
- 238000007599 discharging Methods 0.000 claims description 5
- 239000004571 lime Substances 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 5
- 239000003795 chemical substances by application Substances 0.000 claims description 4
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 3
- 239000011574 phosphorus Substances 0.000 description 3
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 229910021540 colemanite Inorganic materials 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 229910052595 hematite Inorganic materials 0.000 description 2
- 239000011019 hematite Substances 0.000 description 2
- LIKBJVNGSGBSGK-UHFFFAOYSA-N iron(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Fe+3].[Fe+3] LIKBJVNGSGBSGK-UHFFFAOYSA-N 0.000 description 2
- 229910001338 liquidmetal Inorganic materials 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
Images
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
- 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
-
- 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
- C21C5/34—Blowing through the bath
Definitions
- the present invention relates to a pig iron refining process and more specifically to refining phosphorus containing pig iron in a tiltable refining vessel.
- the blowing of oxygen into the molten pig iron in the converter through one or more side tuyeres located in the lateral wall of the converter and below the normal upper level of the liquid metal has been proposed instead of being located in the converter bottom.
- the refining gas is blown through one or more tuyeres in the converter side wall and the jet of refining gas is surrounded by a fluid protecting the converter lining against the corrosive action of the oxygen jet at the region where it discharges into the melt.
- the object of the present invention is a pig iron refining process and specifically for refining phosphorus pig iron, which is carried out with a tipping converter equipped with at least one side tuyere having dual, coaxial conduits.
- the process of the present invention comprises a first stage consisting of: (l charging the converter with liquid iron, with scrap iron and advantageously with lime in powder or blocks; and (2) blowing a highly oxidizing gas which may contain powdered slag forming agents through the central conduit of the side tuyere(s), and in blowing simultaneously a protective fluid through the peripheral tube of the tuyere(s), both fluids discharging below the upper level of the liquid metal surface, during a first stage in which the converter is substantially vertical. This procedure is continued until a carbon content close to the desired final one is achieved.
- blowing is performed through the central conduit of the side tuyere(s) in the side wall and onto the metal bath with a highly oxidizing gas jet capable of penetrating the slag and the metal through the slag while simultaneously blowing a protective fluid through the pe ripheral conduit of the said tuyere(s).
- FIGS. 1 and 2 are schematic representations of the first and second stages of the process described above showing the convertor in a vertical position and in a horizontal position, respectively. It will be understood that the tipping convertor can be further tilted for dis charging the contents of the convertor after refining is completed.
- EXAMPLE I A pig iron containing 3.6% C, 0.3% Si, 0.3% Mn and 1.8% P, balance Fe except for incidental impurities was charged into a 35 ton convertor. The melt was at about l,240C. The charge consisted of 29 tons of the stated pig iron, 10 tons of scrap, 2.7 tons of powdered lime and 200 Kg. of colemanite as a flux.
- the oxygen blow is as follows: a. In a first phase with the convertor vertical, 1,30 Nm were blown in through a side tuyere at the rate of Nm lmirr, for 13 minutes. The oxygen was introduced through a high chromium steel pipe. The oxygen stream was shielded by 3.6 Nm of propane blown in as a jacket around the oxygen, through a larger pipe concentric with the oxygen pipe, at a flow rate of about 3.6
- the final metal analyzed 0.575%C and 0.026%P, and had a temperature of about 1,62.0C. Approximately 24% of the iron was oxidized and recovered as slag.
- the resulting product contained 0.6% C and 0.012% P and had a temperature of about. 1,610C. About 9% iron was oxidized in the slag.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Carbon Steel Or Casting Steel Manufacturing (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| BE782186A BE782186A (fr) | 1972-04-14 | 1972-04-14 | Procede d'affinage de fonte. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3856510A true US3856510A (en) | 1974-12-24 |
Family
ID=3859555
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US00347521A Expired - Lifetime US3856510A (en) | 1972-04-14 | 1973-04-03 | Pig iron refining process |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US3856510A (cs) |
| BE (1) | BE782186A (cs) |
| FR (1) | FR2180132B3 (cs) |
| LU (1) | LU67353A1 (cs) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3972708A (en) * | 1973-09-13 | 1976-08-03 | Verfahrenstechnik Dr.-Ing. Kurt Baum | Process for avoiding formation of smoke and flames in bottom blown converters |
| US4002467A (en) * | 1974-01-30 | 1977-01-11 | Verfahrenstechnik Dr.-Ing. Kurt Baum | Method for recovering reaction gases from steel converters which are bottom blown with oxygen and cooled with hydrocarbons |
| WO2019158479A1 (en) * | 2018-02-16 | 2019-08-22 | Sms Group Gmbh | Method for refining molten metal using a converter |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2855293A (en) * | 1955-03-21 | 1958-10-07 | Air Liquide | Method and apparatus for treating molten metal with oxygen |
| US2875037A (en) * | 1953-03-17 | 1959-02-24 | Pennsylvania Engineering Corp | Method of making bessemer or converter steel |
| FR1450718A (fr) * | 1965-07-12 | 1966-06-24 | Air Liquide | Perfectionnements à des procédés métallurgiques |
| US3313619A (en) * | 1961-03-24 | 1967-04-11 | Lorraine Laminage | Iron refining processes |
| US3330645A (en) * | 1962-08-07 | 1967-07-11 | Air Liquide | Method and article for the injection of fluids into hot molten metal |
| US3706549A (en) * | 1968-02-24 | 1972-12-19 | Maximilianshuette Eisenwerk | Method for refining pig-iron into steel |
-
1972
- 1972-04-14 BE BE782186A patent/BE782186A/xx unknown
-
1973
- 1973-04-03 US US00347521A patent/US3856510A/en not_active Expired - Lifetime
- 1973-04-03 LU LU67353A patent/LU67353A1/xx unknown
- 1973-04-11 FR FR7314047A patent/FR2180132B3/fr not_active Expired
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2875037A (en) * | 1953-03-17 | 1959-02-24 | Pennsylvania Engineering Corp | Method of making bessemer or converter steel |
| US2855293A (en) * | 1955-03-21 | 1958-10-07 | Air Liquide | Method and apparatus for treating molten metal with oxygen |
| US3313619A (en) * | 1961-03-24 | 1967-04-11 | Lorraine Laminage | Iron refining processes |
| US3330645A (en) * | 1962-08-07 | 1967-07-11 | Air Liquide | Method and article for the injection of fluids into hot molten metal |
| FR1450718A (fr) * | 1965-07-12 | 1966-06-24 | Air Liquide | Perfectionnements à des procédés métallurgiques |
| US3706549A (en) * | 1968-02-24 | 1972-12-19 | Maximilianshuette Eisenwerk | Method for refining pig-iron into steel |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3972708A (en) * | 1973-09-13 | 1976-08-03 | Verfahrenstechnik Dr.-Ing. Kurt Baum | Process for avoiding formation of smoke and flames in bottom blown converters |
| US4002467A (en) * | 1974-01-30 | 1977-01-11 | Verfahrenstechnik Dr.-Ing. Kurt Baum | Method for recovering reaction gases from steel converters which are bottom blown with oxygen and cooled with hydrocarbons |
| WO2019158479A1 (en) * | 2018-02-16 | 2019-08-22 | Sms Group Gmbh | Method for refining molten metal using a converter |
Also Published As
| Publication number | Publication date |
|---|---|
| FR2180132B3 (cs) | 1976-04-02 |
| BE782186A (fr) | 1972-04-28 |
| LU67353A1 (cs) | 1973-06-18 |
| FR2180132A1 (cs) | 1973-11-23 |
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