US3700429A - Method of controlling vacuum decarburization - Google Patents
Method of controlling vacuum decarburization Download PDFInfo
- Publication number
- US3700429A US3700429A US751A US3700429DA US3700429A US 3700429 A US3700429 A US 3700429A US 751 A US751 A US 751A US 3700429D A US3700429D A US 3700429DA US 3700429 A US3700429 A US 3700429A
- Authority
- US
- United States
- Prior art keywords
- pressure
- vessel
- decarburization
- oxidation
- expected
- 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
- 238000005261 decarburization Methods 0.000 title abstract description 42
- 238000000034 method Methods 0.000 title abstract description 28
- 238000006243 chemical reaction Methods 0.000 abstract description 27
- 238000007254 oxidation reaction Methods 0.000 abstract description 26
- 230000003647 oxidation Effects 0.000 abstract description 25
- 230000008569 process Effects 0.000 abstract description 13
- 229910000831 Steel Inorganic materials 0.000 abstract description 9
- 239000010959 steel Substances 0.000 abstract description 9
- 239000007789 gas Substances 0.000 description 21
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 14
- 239000001301 oxygen Substances 0.000 description 14
- 229910052760 oxygen Inorganic materials 0.000 description 14
- 239000000203 mixture Substances 0.000 description 12
- 229910052751 metal Inorganic materials 0.000 description 11
- 239000007800 oxidant agent Substances 0.000 description 11
- 239000002184 metal Substances 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 239000000155 melt Substances 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 6
- 238000004364 calculation method Methods 0.000 description 5
- 239000011651 chromium Substances 0.000 description 5
- 230000006872 improvement Effects 0.000 description 5
- 230000001590 oxidative effect Effects 0.000 description 5
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 4
- 229910052804 chromium Inorganic materials 0.000 description 4
- 230000001276 controlling effect Effects 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000012544 monitoring process Methods 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- LIVNPJMFVYWSIS-UHFFFAOYSA-N silicon monoxide Chemical compound [Si-]#[O+] LIVNPJMFVYWSIS-UHFFFAOYSA-N 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 229910044991 metal oxide Inorganic materials 0.000 description 3
- 238000005086 pumping Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 229910000851 Alloy steel Inorganic materials 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910016287 MxOy Inorganic materials 0.000 description 1
- 229910014224 MyOx Inorganic materials 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000010960 commercial process Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000004868 gas analysis Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000002250 progressing effect Effects 0.000 description 1
- 206010037844 rash Diseases 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 238000009628 steelmaking Methods 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
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/10—Handling in a vacuum
Definitions
- ABSTRACT OF THE DISCLOSURE A method of controlling vacuum decarburization of molten steel wherein the ambient pressure within the vessel within which the decarburization is being performed is monitored and compared with an expected pressure calculated from known decarburization reaction parameters to reflect the effectiveness of the decarburization process and the pressure within the vessel or inputs to the reaction are readjusted in order to establish an efficient decarburization reaction while minimizing the oxidation of desired metallic values within the steel.
- This invention relates to the process control of molten metal vacuum decarburization systems where the low pressure (subatmospheric) and a mixture of oxidizing and/or inert gases are used to minimize metallic oxidation.
- vacuum decarburization refers to decarburization systems using subatmospheric pressure.
- the use of low pressure to promote decarburization of steel and its alloys is well known.
- U.S. Pat. No. 2,040,566 suggests that alloy steel may be decarburized under vacuum without the oxidation of metallics.
- vacuum decarburization has not become a commercial process for the decarburization of steels. It is suggested that lack of a responsive method of controlling the reaction has prevented commercial exploitation of the vacuum decarburization process.
- the basic objective of the invention is to control the oxidation of carbon from the melt during vacuum processes.
- the reaction is controlled'in a manner such that excessive build up of easily reducible oxides such as iron and chromium does not occur during the decarburization process.
- oxygen or other oxidizers may be added to a melt at a pressure calculated from thermodynamic considerations. It is also taught that the addition of oxygen or oxidizers is terminated when the pressure within the vessel suddenly increases. This teaching presumes that once the thermodynamic considerations are met, the desired reactions will proceed and no kinetic considerations need be applied.
- oxidizer Reducing pressure in the system accelerates the decarburization reaction and thus, may reduce the metallic oxidation reactions, thereby reducing the metallic losses.
- the supply of oxidizer might also be reduced (oxygen), thereby reducing the amount of oxidizer available for the decarburization reaction to a point in which the oxidizer is essentially totally consumed by that reaction, leaving none available for the oxidation of the metallic values sought to be minimized.
- both the ballast supply and the oxidizer supply may be reduced together to accomplish a combination of the above described effects.
- ballast load Upon the observation of an actual pressure less than the expected pressure indicating metallic oxidation, I prefer to reduce the ballast load gradually, comparing the difierence between new actual and expected pressures (by computing expected pressured for each new ballast load supplied to the system) until reaching a pressure which the system indicates effective decarburization is occurring. This would be where the system pressure was reduced sufi'iciently to a point Where the actual pressure existing within the vessel equaled or exceeded the expected pressure by calculation of the thermodynamic considerations of the decarburization reaction.
- Reference numeral 2 indicates a vessel such as a basic oxygen furnace or a processing ladle containing a bath of molten metal 3 and having a sealed covering 4 attached thereto such that a vacuum may be drawn within the vessel.
- a supply tube 6 is provided for feeding an oxidizer such as oxygen into the vessel and supply tube 8 is provided for feeding a gaseous ballast load such as nitrogen or argon to the interior of the vessel 2.
- a vacuum pump such as a steam ejector system 10, capable of providing a vacuum to the vessel 2 to support efiicient decarburization of the bath 3 within vessel 2.
- a double connected steam ejector system having a main line vacuum 12 and a secondary line vacuum line 14 connected to the vessel 2 such as at cover 4.
- the steam ejector system I employ is a multiple ejector system having a single first stage 16, a double section stage 18 and 18' coupled directly to the first stage 16 and each of which are connected to a steam condenser 20.
- a ballast supply 22 is provided to first condenser 20.
- Third stage ejectors 24, 24' and 24" are connected to condenser and directly to ejectors 18 and 18.
- Third stage ejectors 24 and 25 are individually connected to second stage condensers 26 and 26' which are in turn connected to fourth stage ejectors 28 and 28'.
- An additional fourth stage ejector 28" is connected directly to the third stage ejector 24. All three of the fourth stage ejectors 28, 28' and 28" are connected to a final stage condenser 30.
- Ballast is supplied to this system at 22 to assist the establishing of a particular desired pressure within the vessel 2 in conjunction with oxidizer supply at 6.
- the ballast supply at 8 is conventionally an emergency nitrogen ballast which may be fed directly into the vessel.
- This same nitrogen ballast system may be used for back-filling the reaction a system when the decarburization and other gasing cycles are completed. It is possible to supply the ballast load for regulating the ambient pressure of the system through supply 8 though practical advantage is gained at 22.
- the decarburization apparatus would also include flow measurement and control devices 32 in the oxidizer supply system being capable of measuring the flow of the oxidizer and control therefor, as well as any inert gases which may be also injected therein. Vacuum pressure gauges will be provided as at 34 to measure the vacuum within the vessel, as well as desirable control points within the steam ejector system such as preceding each ejector stage.
- 01f gas analysis system is provided as is known in the art for measuring the particular off gases and the composition of the off gas according to its components.
- similar flow control and measuring devices are necessary in line 22 as at 36 for the measure and control of the ballast supplied through line 22.
- Suitable control and measuring means are commercially available and known in the art. It is also preferable to have a computer available to perform the calculation of the decarburization reaction to rapidly provide the calculation of the expected pressure according to the various parameters estab- 50 lished within the system.
- maintaining said actual vessel pressure at least as great as said expected pressure includes reducing the quantity of oxidizing material introduced into the vesel while maintaining the flow rate of input gases constant, thereby maintaining a constant ambient pressure within said vessel.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Treatment Of Steel In Its Molten State (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US75170A | 1970-01-05 | 1970-01-05 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3700429A true US3700429A (en) | 1972-10-24 |
Family
ID=21692872
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US751A Expired - Lifetime US3700429A (en) | 1970-01-05 | 1970-01-05 | Method of controlling vacuum decarburization |
Country Status (10)
| Country | Link |
|---|---|
| US (1) | US3700429A (enExample) |
| JP (1) | JPS5543047B1 (enExample) |
| AT (1) | AT318675B (enExample) |
| BE (1) | BE760724A (enExample) |
| CA (1) | CA946163A (enExample) |
| DE (1) | DE2061122C3 (enExample) |
| ES (1) | ES386534A1 (enExample) |
| FR (1) | FR2075921B1 (enExample) |
| GB (1) | GB1335397A (enExample) |
| SE (1) | SE392733B (enExample) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3847593A (en) * | 1971-07-13 | 1974-11-12 | Centro Speriment Metallurg | Process for refining metals, in particular liquid pig iron, in oxygen converters with continuous control of the operative procedure |
| US4251269A (en) * | 1977-09-10 | 1981-02-17 | Nisshin Steel Co., Ltd. | Method for controlling steel making process under reduced pressures |
| US4427443A (en) | 1979-11-28 | 1984-01-24 | Etude Et Developpement En Metallurgie | Process and apparatus for automating a vacuum degasification cycle for metal alloys |
| US5417739A (en) * | 1993-12-30 | 1995-05-23 | Ltv Steel Company, Inc. | Method of making high nitrogen content steel |
| US5618490A (en) * | 1992-12-18 | 1997-04-08 | Mannesmann Aktiengesellschaft | Vacuum installation, in particular for recycling metallurgy |
| US5830259A (en) * | 1996-06-25 | 1998-11-03 | Ltv Steel Company, Inc. | Preventing skull accumulation on a steelmaking lance |
| US5865876A (en) * | 1995-06-07 | 1999-02-02 | Ltv Steel Company, Inc. | Multipurpose lance |
| US5885323A (en) * | 1997-04-25 | 1999-03-23 | Ltv Steel Company, Inc. | Foamy slag process using multi-circuit lance |
| WO2006067365A1 (en) * | 2004-12-20 | 2006-06-29 | The Boc Group Plc | Method of degassing molten metal |
| US20090123414A1 (en) * | 2004-12-13 | 2009-05-14 | Cytos Biotechnology Ag | Il-15 Antigen Arrays And Uses Thereof |
| CN115124161A (zh) * | 2022-05-13 | 2022-09-30 | 华能山东发电有限公司烟台发电厂 | 一种延长发电机转子冷却水处理装置树脂使用周期的方法 |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2438122A1 (de) * | 1974-08-08 | 1976-02-19 | Witten Edelstahl | Verfahren zum vakuumentkohlen von metallschmelzen |
| JPS569319A (en) * | 1979-07-05 | 1981-01-30 | Nippon Steel Corp | Vacuum treatment controller for molten steel |
| US4541862A (en) * | 1982-11-30 | 1985-09-17 | A. Finkl & Sons Co. | Ladle steelmaking method and apparatus |
| RU2064660C1 (ru) * | 1993-12-06 | 1996-07-27 | Акционерное общество "Нижнетагильский металлургический комбинат" | Устройство для контроля состояния зеркала расплавленного металла |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR1343235A (fr) * | 1962-12-21 | 1963-11-15 | Nippon Kokan Kk | Procédé pour la production de ferrochrome sans carbone |
| US3420657A (en) * | 1966-02-14 | 1969-01-07 | Union Carbide Corp | Oxygen treatment of chromium alloys |
-
1970
- 1970-01-05 US US751A patent/US3700429A/en not_active Expired - Lifetime
- 1970-12-11 DE DE2061122A patent/DE2061122C3/de not_active Expired
- 1970-12-14 AT AT1120370A patent/AT318675B/de active
- 1970-12-16 ES ES386534A patent/ES386534A1/es not_active Expired
- 1970-12-21 FR FR7046098A patent/FR2075921B1/fr not_active Expired
- 1970-12-22 CA CA101,226A patent/CA946163A/en not_active Expired
- 1970-12-23 BE BE760724A patent/BE760724A/xx unknown
- 1970-12-29 GB GB6157370A patent/GB1335397A/en not_active Expired
- 1970-12-29 SE SE7017674A patent/SE392733B/xx unknown
-
1971
- 1971-01-04 JP JP1271A patent/JPS5543047B1/ja active Pending
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3847593A (en) * | 1971-07-13 | 1974-11-12 | Centro Speriment Metallurg | Process for refining metals, in particular liquid pig iron, in oxygen converters with continuous control of the operative procedure |
| US4251269A (en) * | 1977-09-10 | 1981-02-17 | Nisshin Steel Co., Ltd. | Method for controlling steel making process under reduced pressures |
| US4427443A (en) | 1979-11-28 | 1984-01-24 | Etude Et Developpement En Metallurgie | Process and apparatus for automating a vacuum degasification cycle for metal alloys |
| US5618490A (en) * | 1992-12-18 | 1997-04-08 | Mannesmann Aktiengesellschaft | Vacuum installation, in particular for recycling metallurgy |
| US5417739A (en) * | 1993-12-30 | 1995-05-23 | Ltv Steel Company, Inc. | Method of making high nitrogen content steel |
| US5865876A (en) * | 1995-06-07 | 1999-02-02 | Ltv Steel Company, Inc. | Multipurpose lance |
| US5830259A (en) * | 1996-06-25 | 1998-11-03 | Ltv Steel Company, Inc. | Preventing skull accumulation on a steelmaking lance |
| US5885323A (en) * | 1997-04-25 | 1999-03-23 | Ltv Steel Company, Inc. | Foamy slag process using multi-circuit lance |
| US20090123414A1 (en) * | 2004-12-13 | 2009-05-14 | Cytos Biotechnology Ag | Il-15 Antigen Arrays And Uses Thereof |
| WO2006067365A1 (en) * | 2004-12-20 | 2006-06-29 | The Boc Group Plc | Method of degassing molten metal |
| US20080034922A1 (en) * | 2004-12-20 | 2008-02-14 | Bruce Simon H | Method of Degassing Molten Metal |
| MD3997C2 (ro) * | 2004-12-20 | 2010-07-31 | Edwards Limited | Dispozitiv şi procedeu de degazare a metalului topit (variante) |
| US7815845B2 (en) | 2004-12-20 | 2010-10-19 | Edwards Limited | Method of degassing molten metal |
| CN115124161A (zh) * | 2022-05-13 | 2022-09-30 | 华能山东发电有限公司烟台发电厂 | 一种延长发电机转子冷却水处理装置树脂使用周期的方法 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5543047B1 (enExample) | 1980-11-04 |
| GB1335397A (en) | 1973-10-24 |
| DE2061122B2 (de) | 1981-07-30 |
| DE2061122C3 (de) | 1982-11-25 |
| BE760724A (fr) | 1971-06-23 |
| DE2061122A1 (de) | 1971-07-15 |
| FR2075921A1 (enExample) | 1971-10-15 |
| FR2075921B1 (enExample) | 1974-09-20 |
| AT318675B (de) | 1974-11-11 |
| CA946163A (en) | 1974-04-30 |
| ES386534A1 (es) | 1973-11-16 |
| SE392733B (sv) | 1977-04-18 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AS | Assignment |
Owner name: ALLEGHENY LUDLUM CORPORATION Free format text: CHANGE OF NAME;ASSIGNOR:ALLEGHENY LUDLUM STEEL CORPORATION;REEL/FRAME:004779/0642 Effective date: 19860805 |
|
| AS | Assignment |
Owner name: PITTSBURGH NATIONAL BANK Free format text: SECURITY INTEREST;ASSIGNOR:ALLEGHENY LUDLUM CORPORATION;REEL/FRAME:004855/0400 Effective date: 19861226 |
|
| AS | Assignment |
Owner name: PITTSBURGH NATIONAL BANK Free format text: ASSIGNMENT OF ASSIGNORS INTEREST. RECORDED ON REEL 4855 FRAME 0400;ASSIGNOR:PITTSBURGH NATIONAL BANK;REEL/FRAME:005018/0050 Effective date: 19881129 |