US1709389A - Bessemer process of making steel - Google Patents
Bessemer process of making steel Download PDFInfo
- Publication number
- US1709389A US1709389A US717282A US71728224A US1709389A US 1709389 A US1709389 A US 1709389A US 717282 A US717282 A US 717282A US 71728224 A US71728224 A US 71728224A US 1709389 A US1709389 A US 1709389A
- Authority
- US
- United States
- Prior art keywords
- heat
- bessemer
- amount
- making steel
- 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
- 238000009618 Bessemer process Methods 0.000 title description 4
- 229910000831 Steel Inorganic materials 0.000 title description 4
- 239000010959 steel Substances 0.000 title description 4
- 238000000034 method Methods 0.000 description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 11
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 6
- 229910052698 phosphorus Inorganic materials 0.000 description 6
- 239000011574 phosphorus Substances 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 239000002699 waste material Substances 0.000 description 5
- 239000012535 impurity Substances 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 229910052710 silicon Inorganic materials 0.000 description 3
- 239000010703 silicon Substances 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- 229910000805 Pig iron Inorganic materials 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910000389 calcium phosphate Inorganic materials 0.000 description 1
- 239000001506 calcium phosphate Substances 0.000 description 1
- 235000011010 calcium phosphates Nutrition 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- XWHPIFXRKKHEKR-UHFFFAOYSA-N iron silicon Chemical compound [Si].[Fe] XWHPIFXRKKHEKR-UHFFFAOYSA-N 0.000 description 1
- 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 1
- 238000004519 manufacturing process Methods 0.000 description 1
- DPTATFGPDCLUTF-UHFFFAOYSA-N phosphanylidyneiron Chemical compound [Fe]#P DPTATFGPDCLUTF-UHFFFAOYSA-N 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 description 1
- 239000002912 waste gas 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
- 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
- FRANK W..DAVIS or mrnronn, DELAWARE, "assrenon To seminar. a. ALLEN, TRUSTEE.
- the impurities of the iron, carbon, manganese, silicon and, in the basic process, phosphorus are oxidized, having as a prod not, nearly pure iron.
- the oxidation of the impurities generates the heat necessary for the process.
- silicon 15 contributes largely to the heat generated,
- this process will enable the operator to finish his metal at a high temperature without danger of over oxidation.
- he may impartsufficient temperature to the steel to permit of its being allowed to stand in the ladle a considerable time before teeming.
- Molten steel which is permitted-to stand in this manner will be of a better grade inthat a considerable portion of the included impurities will have the opplertunity to, rise to the surface with the slag There is thus a. time factor not heretofore available, while in addition the metal "is more fluid so that the impurities in suspension may rise more readily.
- the Bessemer process is improved.
- the slag so formed will have an appreciable amount of calcium phosphate and may be utilized as a fertilizer.
- I claim: 1. The method of carrying out the Bessem r process of making steel with noneBesse-' Imer pig which consists in enriching the blast air with oxygen in an amount sufficient to reduce the proportion of nitrogen in the blast in an amount such that the nitrogen absorbs only an allowable proportion of the a heat so' that the net heat of the blow will satisfy the requirements.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Fertilizers (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Description
Patented Apr. 16, 1 929.
UNITED STATES PATENT-OFFICE.
FRANK W..DAVIS, or mrnronn, DELAWARE, "assrenon To seminar. a. ALLEN, TRUSTEE.
nnssmm'a rnocnss or MAKING STEEL.
No Drawing.
action of numerous jets of air blown through it, the impurities of the iron, carbon, manganese, silicon and, in the basic process, phosphorus are oxidized, having as a prod not, nearly pure iron. The oxidation of the impurities generates the heat necessary for the process. In the acid process, silicon 15 contributes largely to the heat generated,
and in the basic process, phosphorus is the big factor. This means that for successful operation ofthe Bessemer process, we must use a pig iron high in eithersilica or phos- 2o phorus, depending upon whether it is acid or basic. High silicon iron requiring higher fuel consumption in the blast furnace, demands a correspondingly high price, while high phosphorus iron is not available in the United States in suflicient quantities to make possible a' basic Bessemer industry.
Over fifty percent of the total heat developed by the reactions in the Bessemer process is "lost as sensible heat in the waste gases. Any method therefor which will make possible. decreasing at will the quantity of this as, (and,.therefore,'the loss of sensible heat By waste) will first lower materially the chemibal requirements of the iron, i. e., in the acid process, the silicon, and in the basic, the phosphorus. That is to say, the process may be carried out with what are now known as non-Bessemer pig. Further, it will relieve the operator from the necessity of 40 mixing various grades of pig iron in order to start with a more or less definite chemical analysis, as instead of regulating the amount of heat generated, he will now regulate or secure the temperature of his bath by regulating the amount of heat carried away in his gases. My process, therefore, consists in determining the netblow heat required in any given case and in' so regulatlng thev amount of heat which is wasted as to secure the neces- Application filed June 2, 1924. Serial No. 717,282.
sary net blow heat. This 'is done through decreasing the amount of nitrogen in the blast, whereby the waste nitrogen gases will not carry away more than the allowable proportion of heat, as waste.
It is preferred to obtain the above effects and advantages by regulating the oxygen content of the blast. This will be accomplished by enrichingthe air to any percentage oxygen desired, prior to its passage through the converter. The oxygen will reduce the proportion of nitrogen in the blast and hence the volume of waste nitrogen gas, the amount of which may be thus controlled.
In addition to the above mentioned features, this process will enable the operator to finish his metal at a high temperature without danger of over oxidation. By this practice, he may impartsufficient temperature to the steel to permit of its being allowed to stand in the ladle a considerable time before teeming. Molten steel which is permitted-to stand in this manner will be of a better grade inthat a considerable portion of the included impurities will have the opplertunity to, rise to the surface with the slag There is thus a. time factor not heretofore available, while in addition the metal "is more fluid so that the impurities in suspension may rise more readily. Hence, 30 the Bessemer process is improved.
Further, in the case of the basic process in which phosphorus is eliminated from the bath, the slag so formed will have an appreciable amount of calcium phosphate and may be utilized as a fertilizer.
I claim: 1. The method of carrying out the Bessem r process of making steel with noneBesse-' Imer pig which consists in enriching the blast air with oxygen in an amount sufficient to reduce the proportion of nitrogen in the blast in an amount such that the nitrogen absorbs only an allowable proportion of the a heat so' that the net heat of the blow will satisfy the requirements.
2. The method of making ahigh phosphorus slag which may be used for fertilizer, when using an iron in which the. phosphorus is too low to be classed as a basic Bessemer 1 amount of oxygen to the amount of inert gases in theblast so as to reduce the heat in the waste to the point which will give them blow heat required.
In testimony whereof, I have hereunto signed my name.
FRANK W. DAVIS.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US717282A US1709389A (en) | 1924-06-02 | 1924-06-02 | Bessemer process of making steel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US717282A US1709389A (en) | 1924-06-02 | 1924-06-02 | Bessemer process of making steel |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1709389A true US1709389A (en) | 1929-04-16 |
Family
ID=24881402
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US717282A Expired - Lifetime US1709389A (en) | 1924-06-02 | 1924-06-02 | Bessemer process of making steel |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1709389A (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE746980C (en) * | 1939-08-02 | 1944-09-01 | H A Brassert & Co | Process for making low-nitrogen steel by wind refining |
| US2480044A (en) * | 1945-04-23 | 1949-08-23 | Florence Stove Co | Range oven vent |
| US2502259A (en) * | 1946-12-12 | 1950-03-28 | Air Reduction | Method of eliminating carbon from and controlling the temperature of molten steel |
| US2529387A (en) * | 1943-07-12 | 1950-11-07 | Stora Kopparbergs Bergslags Ab | Method of producing bessemer steel |
| US2584151A (en) * | 1947-11-12 | 1952-02-05 | Nat Steel Corp | Method of blowing ferrous metal |
| DE763238C (en) * | 1938-03-06 | 1953-01-26 | August Thyssen Huette A G | Process for the production of Thomasstahl with nitrogen contents below 0.01% |
| US2649366A (en) * | 1951-11-02 | 1953-08-18 | Jordan James Fernando | Profile method of making steel |
| US2671018A (en) * | 1952-03-31 | 1954-03-02 | Huettenwerk Oberhausen Ag | Process for the production of basic bessemer steel low in nitrogen |
| US2707677A (en) * | 1952-03-27 | 1955-05-03 | Huettenwerk Oberhausen Ag | Method of making steel with a low nitrogen content by the converter process |
| USRE31676E (en) * | 1982-09-29 | 1984-09-18 | Thyssen Aktiengesellschaft vorm August Thyssen-Hutte AG | Method and apparatus for dispensing a fluidizable solid from a pressure vessel |
-
1924
- 1924-06-02 US US717282A patent/US1709389A/en not_active Expired - Lifetime
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE763238C (en) * | 1938-03-06 | 1953-01-26 | August Thyssen Huette A G | Process for the production of Thomasstahl with nitrogen contents below 0.01% |
| DE746980C (en) * | 1939-08-02 | 1944-09-01 | H A Brassert & Co | Process for making low-nitrogen steel by wind refining |
| US2529387A (en) * | 1943-07-12 | 1950-11-07 | Stora Kopparbergs Bergslags Ab | Method of producing bessemer steel |
| US2480044A (en) * | 1945-04-23 | 1949-08-23 | Florence Stove Co | Range oven vent |
| US2502259A (en) * | 1946-12-12 | 1950-03-28 | Air Reduction | Method of eliminating carbon from and controlling the temperature of molten steel |
| US2584151A (en) * | 1947-11-12 | 1952-02-05 | Nat Steel Corp | Method of blowing ferrous metal |
| US2649366A (en) * | 1951-11-02 | 1953-08-18 | Jordan James Fernando | Profile method of making steel |
| US2707677A (en) * | 1952-03-27 | 1955-05-03 | Huettenwerk Oberhausen Ag | Method of making steel with a low nitrogen content by the converter process |
| US2671018A (en) * | 1952-03-31 | 1954-03-02 | Huettenwerk Oberhausen Ag | Process for the production of basic bessemer steel low in nitrogen |
| USRE31676E (en) * | 1982-09-29 | 1984-09-18 | Thyssen Aktiengesellschaft vorm August Thyssen-Hutte AG | Method and apparatus for dispensing a fluidizable solid from a pressure vessel |
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