USRE18609E - Charles habt - Google Patents
Charles habt Download PDFInfo
- Publication number
- USRE18609E USRE18609E US18609DE USRE18609E US RE18609 E USRE18609 E US RE18609E US 18609D E US18609D E US 18609DE US RE18609 E USRE18609 E US RE18609E
- Authority
- US
- United States
- Prior art keywords
- ore
- chromium
- nickel
- ores
- 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
Links
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 36
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 30
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 22
- 229910052804 chromium Inorganic materials 0.000 description 22
- 239000011651 chromium Substances 0.000 description 22
- 229910052759 nickel Inorganic materials 0.000 description 18
- 229910052742 iron Inorganic materials 0.000 description 15
- 229910052751 metal Inorganic materials 0.000 description 14
- 239000002184 metal Substances 0.000 description 14
- 238000000034 method Methods 0.000 description 11
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 7
- 229910052726 zirconium Inorganic materials 0.000 description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 229910000831 Steel Inorganic materials 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 150000002739 metals Chemical class 0.000 description 6
- 239000010959 steel Substances 0.000 description 6
- 229910045601 alloy Inorganic materials 0.000 description 5
- 239000000956 alloy Substances 0.000 description 5
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 4
- 239000000460 chlorine Substances 0.000 description 4
- 229910052801 chlorine Inorganic materials 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
- 150000001805 chlorine compounds Chemical class 0.000 description 3
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 238000007792 addition Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- TXWRERCHRDBNLG-UHFFFAOYSA-N cubane Chemical compound C12C3C4C1C1C4C3C12 TXWRERCHRDBNLG-UHFFFAOYSA-N 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical class [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- FBAFATDZDUQKNH-UHFFFAOYSA-M iron chloride Chemical compound [Cl-].[Fe] FBAFATDZDUQKNH-UHFFFAOYSA-M 0.000 description 1
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 1
- 239000011504 laterite Substances 0.000 description 1
- 229910001710 laterite Inorganic materials 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
- NDLPOXTZKUMGOV-UHFFFAOYSA-N oxo(oxoferriooxy)iron hydrate Chemical compound O.O=[Fe]O[Fe]=O NDLPOXTZKUMGOV-UHFFFAOYSA-N 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/02—Roasting processes
- C22B1/08—Chloridising roasting
Definitions
- the process is applicable to many ores con taining two or more different kinds of metal
- Chromium and nickel, as found in these ores are found to be less readily chloridized, than is iron, and the process accordingly embraces the step of heating the ore to a temperature at which chloridization of the ore can be effected, say by means of chlorine gas of a gas containing chlorine (which may be in the elemental COIlClltlOIl if desired) although it is possible to effect the chloridization by other methods, although probably less advantageously.
- a quantity of ore is placed in a retort,'and
- stream of gas containing free chlorine is assed' through the charge of ore so heated.
- ' l ore or less'reducing agent may be added at the beginning of the operation, which will assist in the chloridization of the ore, by the method set forth. Under these conditions, a substantial portion of the iron content of the ore will vaporize, and after continuing the treatment for about an hour and a-half, it
- the material vaporized in the form ;of chlorides but under the preferred temperature conditions, the material vaporized will be largely iron, in the form of ferric chloride, accompanied by extremely small amounts of the chlorides of chromium and nickel, so that analysis of the ore after the treatment Will show a substantial increase in the ratio of chromium and nickel to iron;
- the charge may be smelted in a suitable furnace, such as a blast furnace, to obtain a hot metal having a comparativel high percentage of chromium and nicke, and optionally zirconium, from which a high grade of rustless steel can be made.
- a suitable furnace such as a blast furnace
- any of the usual blast furnace procedures can be employed, such as first briquetting the ores'if desired, the use of suitable amounts of fuel and fluxing agents, such as lime and the like, or the ore could be reduced in another manner instead of in a blast furnace.
- a process which comprises heating an ore containing iron in large proportion, and chromium and nickel in far smaller quantities which comprises heating said ore to a. temperature at which ferric chloride is readily volatile, and contacting the ore with a stream of gases containing free chlorine until the iron content of the ore has been substantially lowered and the percentages of chromium and nickel content of the ore has been substantially increased and thereafter adding further quantities of chromium and nickel ores, and adding zirconium ore, then reducing the material in a furnace to produce a hot metal which is particularly suitable for the production of alloy steels.
- a process which comprises heating an ore containing iron in large proportion, and chromium in far smaller quantity which comprises heating said ore to a temperature at which ferric chloride is readily volatile, and contacting the ore with a stream of gases containing chlorine until the iron content of the ore has been substantially lowered and the percentage of chromium content 'of the ore has been substantially increased, thereafter adding a further quantity of chromium ore, adding zirconium and reducing the material in a furnaceto produce a hot metal which is particularly suitable for the production of alloy steels.
- a process for treating ores containing iron in large proportions and other metals in smaller quantities which consists in heating the ore to a suitable temperature in the presence of a chloridizing agent until the percentage of iron inthe ore has been substantially lowered andthe percentage of such other metals has been substantially raised,
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
Reiseued Sept. 27, 1932 UNITED STATES PATENT OFFICE CHARLES HART, OF MEDIA, PENNSYLVANIA, ASSIGNOR OF ONE-HALF'TO PETER SHIELDS, WASHINGTON, DISTRICT OF COLUMBIA PROCESS OF TREATING ORES IN THE MANUFACTURE OF RUSTLESS STEEL 1T0 Drawing. Original No. 1,826,932, dated October 13, 1931, Serial No. 484,712, filed September 26, 1930.
Application for reissue filed December 10,'19'31.
5 come partially removed, so that the relative ratio of the second class of metals, to the first class of metals, is increased.
The process is applicable to many ores con taining two or more different kinds of metal,
and a particular ore to which I 'call attention is a Cuban ore, consisting largely of ferric oxide in a hydrated condition. An analysis of this ore' showed one sample to contain about 46% of iron, about 2% of silica, about 8% of alumina, about 1.7% of chromium,
abut 0.5% of nickel, and about 12% of water. Another somewhat similar ore contained around 46.75% of iron, 6% of silica, 12% of alumina, 1.85% of chromium, 1% of nickel and around 11% of water. The ores also contained small amounts of manganese, lime, soda, sulphur compounds and potassium. A similar'ore found in a different loc'atlon is known as laterite. These ores are cited merely as examples of ores which may be treated in accordance with the present invention. Chromium and nickel, as found in these ores are found to be less readily chloridized, than is iron, and the process accordingly embraces the step of heating the ore to a temperature at which chloridization of the ore can be effected, say by means of chlorine gas of a gas containing chlorine (which may be in the elemental COIlClltlOIl if desired) although it is possible to effect the chloridization by other methods, although probably less advantageously. Reducing the ore, for the production of hot metal from which stainless steel can readily be produced by a direct method, is not readily possible for the reason that the content of chromium and nickel in theore is insufiic ient and it is not always readily possible to enrich the hot metal in chromium and nickel, to the required extent.
Accordingly I give the following method by which this result can readily be secured.
A quantity of ore is placed in a retort,'and
is heated in any suitable manner to a tem- Serial No. 580,230
stream of gas containing free chlorine is assed' through the charge of ore so heated.
' l ore or less'reducing agent may be added at the beginning of the operation, which will assist in the chloridization of the ore, by the method set forth. Under these conditions, a substantial portion of the iron content of the ore will vaporize, and after continuing the treatment for about an hour and a-half, it
will be found that there has been a material change in the ratio between iron present and nickel and chromium present, due to the volatilization of iron chloride from the ore. It will beiunderstood that the volatilization is somewhat more rapid at temperatures sub stantially higher than here indicated, but there is likely to be more loss of the chromium and nickel, by volatilization. In this connection it may be noted that both chromium and, nickel are capable of conversion into chlorides and. vaporization in the form ;of chlorides, but under the preferred temperature conditions, the material vaporized will be largely iron, in the form of ferric chloride, accompanied by extremely small amounts of the chlorides of chromium and nickel, so that analysis of the ore after the treatment Will show a substantial increase in the ratio of chromium and nickel to iron;
Having thus concentrated the ores in chromium and nickel, other materials suitable for furnishing alloy constituents may be added, these being added either in the form of crude ores or concentrates. For example, after the chloridization treatment, other chromium ores can be added to the ore, and other nickel ores can be added. I also contemplate adding ores of other metals such as zirconium which are useful in the production of alloy steels of the kind referred to. Ordinarily I would not recommend adding the zirconium ores to the initial ore prior to chloridization, for the reason that the chloridization treatment might carry away a substantial proportion of the zirconium, which of course as recognized is relatively high priced material.
After the chloridization treatment and after the addition of other ores as above inperature of between 400 and 500 .C., and a dicated, the charge may be smelted in a suitable furnace, such as a blast furnace, to obtain a hot metal having a comparativel high percentage of chromium and nicke, and optionally zirconium, from which a high grade of rustless steel can be made. It will be understood that any of the usual blast furnace procedures can be employed, such as first briquetting the ores'if desired, the use of suitable amounts of fuel and fluxing agents, such as lime and the like, or the ore could be reduced in another manner instead of in a blast furnace. During the smelting operation, some of the oxide of iron, most of the silica and alumina and perhaps small quantities of the oxides of chromium and nickel might pass into the slag, but the main portions of the chromium and nickel, together with a part of the iron would be reduced to the metallic state, and the zirconium if employed would likewise be reduced to the metallic condition, and would enter the hot metal.
It will be understood that the preferred temperature to be employed in the particular case naturally depends to a considerable extent upon the precise ore under treatment, and experimental runs should be made with each batch of ore to determine the most advantageous temperature for that particular ore. With the Cuban ore according to the -first analysis above given, a temperature of about 4:80 to 490 C. will be found most satisfactory.
I claim:
1. A process which comprises heating an ore containing iron in large proportion, and chromium and nickel in far smaller quantities, which comprises heating said ore to a. temperature at which ferric chloride is readily volatile, and contacting the ore with a stream of gases containing free chlorine until the iron content of the ore has been substantially lowered and the percentages of chromium and nickel content of the ore has been substantially increased and thereafter adding further quantities of chromium and nickel ores, and adding zirconium ore, then reducing the material in a furnace to produce a hot metal which is particularly suitable for the production of alloy steels.
2. A process which comprises heating an ore containing iron in large proportion, and chromium in far smaller quantity, which comprises heating said ore to a temperature at which ferric chloride is readily volatile, and contacting the ore with a stream of gases containing chlorine until the iron content of the ore has been substantially lowered and the percentage of chromium content 'of the ore has been substantially increased, thereafter adding a further quantity of chromium ore, adding zirconium and reducing the material in a furnaceto produce a hot metal which is particularly suitable for the production of alloy steels.
quantities of chromium and nickel ores, and
reducing the wholein a furnace.
4. A process for treating ores containing iron in large proportions and other metals in smaller quantities, which consists in heating the ore to a suitable temperature in the presence of a chloridizing agent until the percentage of iron inthe ore has been substantially lowered andthe percentage of such other metals has been substantially raised,
increasing the percentage of such other metals by additions of the ores thereof to the charge, and smelting the residue to produce a hot metal suitable for the manufacture of alloy steels.
CHARLES HART.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| USRE18609E true USRE18609E (en) | 1932-09-27 |
Family
ID=2082063
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US18609D Expired USRE18609E (en) | Charles habt |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | USRE18609E (en) |
-
0
- US US18609D patent/USRE18609E/en not_active Expired
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US1717160A (en) | Reduction of complex ores | |
| US3502461A (en) | Method of reducing oxidic raw materials | |
| US2395029A (en) | Method of reducing iron ores | |
| US2582469A (en) | Metallurgy | |
| USRE18609E (en) | Charles habt | |
| US1954400A (en) | Process of making rustless iron | |
| US1513735A (en) | Method of manufacturing low-carbon steels | |
| US2313044A (en) | Reduction of ores to metal | |
| US1826932A (en) | Process of treating ores in the manufacture of rustless steel | |
| US1568464A (en) | Method of recovering copper | |
| US2031152A (en) | Manufacture of alloys of iron, chromium, nickel, and copper | |
| US1365091A (en) | Allot | |
| US1431877A (en) | Smelting ores or the like | |
| US1925886A (en) | Manufacture of iron and steel alloys | |
| US3556774A (en) | Process for the reduction of molten iron ore | |
| US2082783A (en) | Method of making alloy steels | |
| US930344A (en) | Process of treating titaniferous iron ores. | |
| US1523044A (en) | Process of reducing ores and obtaining metal products therefrom | |
| US2995455A (en) | Method of recovering nickel and iron from laterite ores by preferential reduction | |
| US1975338A (en) | Process of forming chromium iron alloys | |
| US1613571A (en) | Process of making molybdenum steel | |
| US1543321A (en) | Process for producing metals and alloys | |
| US1401924A (en) | Process of recovering molybdenum from molybdenite | |
| US1596999A (en) | Production of low-carbon iron-chromium alloys | |
| US1833320A (en) | Process of reducing iron ores |