US2221624A - Treatment of manganese alloys - Google Patents
Treatment of manganese alloys Download PDFInfo
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- US2221624A US2221624A US257455A US25745539A US2221624A US 2221624 A US2221624 A US 2221624A US 257455 A US257455 A US 257455A US 25745539 A US25745539 A US 25745539A US 2221624 A US2221624 A US 2221624A
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- manganese
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- sulphur
- boron
- alloys
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- 229910000914 Mn alloy Inorganic materials 0.000 title description 50
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 39
- 239000005864 Sulphur Substances 0.000 description 39
- 229910045601 alloy Inorganic materials 0.000 description 33
- 239000000956 alloy Substances 0.000 description 33
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 24
- 229910052796 boron Inorganic materials 0.000 description 24
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 20
- 229910052748 manganese Inorganic materials 0.000 description 20
- 239000011572 manganese Substances 0.000 description 20
- 235000002908 manganese Nutrition 0.000 description 20
- 229910021538 borax Inorganic materials 0.000 description 13
- 235000010339 sodium tetraborate Nutrition 0.000 description 13
- 239000004328 sodium tetraborate Substances 0.000 description 13
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 description 12
- 150000001639 boron compounds Chemical class 0.000 description 11
- AMWRITDGCCNYAT-UHFFFAOYSA-L manganese oxide Inorganic materials [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 description 11
- 238000000034 method Methods 0.000 description 9
- 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 8
- 230000000694 effects Effects 0.000 description 7
- 238000002156 mixing Methods 0.000 description 7
- 235000010338 boric acid Nutrition 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000000155 melt Substances 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- 229910052783 alkali metal Inorganic materials 0.000 description 3
- -1 alkali metal salts Chemical class 0.000 description 3
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 3
- 239000004327 boric acid Substances 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 239000002585 base Substances 0.000 description 2
- 125000005619 boric acid group Chemical class 0.000 description 2
- 229910052804 chromium Inorganic materials 0.000 description 2
- 239000011651 chromium Substances 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 230000006698 induction Effects 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 150000004760 silicates Chemical class 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 241000556720 Manga Species 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 238000005275 alloying Methods 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910052790 beryllium Inorganic materials 0.000 description 1
- ATBAMAFKBVZNFJ-UHFFFAOYSA-N beryllium atom Chemical compound [Be] ATBAMAFKBVZNFJ-UHFFFAOYSA-N 0.000 description 1
- 150000001638 boron Chemical class 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical compound [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 description 1
- 229910001634 calcium fluoride Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- JKWMSGQKBLHBQQ-UHFFFAOYSA-N diboron trioxide Chemical class O=BOB=O JKWMSGQKBLHBQQ-UHFFFAOYSA-N 0.000 description 1
- UQGFMSUEHSUPRD-UHFFFAOYSA-N disodium;3,7-dioxido-2,4,6,8,9-pentaoxa-1,3,5,7-tetraborabicyclo[3.3.1]nonane Chemical group [Na+].[Na+].O1B([O-])OB2OB([O-])OB1O2 UQGFMSUEHSUPRD-UHFFFAOYSA-N 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- PPNAOCWZXJOHFK-UHFFFAOYSA-N manganese(2+);oxygen(2-) Chemical class [O-2].[Mn+2] PPNAOCWZXJOHFK-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 235000010269 sulphur dioxide Nutrition 0.000 description 1
- 239000004291 sulphur dioxide Substances 0.000 description 1
- 238000006557 surface reaction Methods 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 239000011135 tin Substances 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 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
- C22B9/00—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
- C22B9/10—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals with refining or fluxing agents; Use of materials therefor, e.g. slagging or scorifying agents
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C28/00—Alloys based on a metal not provided for in groups C22C5/00 - C22C27/00
Definitions
- This invention relates to the treatment of manganese alloys and is particularly concerned with the removal of sulphur therefrom in order to provide alloys essentially free of sulphur.
- Electrolytic manganese as prepared in accordance with.
- the sulphur content of the finished alloy will be 0.12% assuming that sulphur has not been introduced into the alloy from any other source. If, however, the manganese content of the alloy is say 90%, then the sulphur content of the finished alloy would be 0.27%. In the usual case,.-the sulphur content of the alloys should be reduced to not substantially in excess of 0;02% and should preferably be substantially less than that or in other words of the order of a few thousandths of a percent.
- the sulphur is effectively removed in a simple and inexpensive manner.
- the removal of the sulphur from the manganese alloys containing the same is efiected by mixing the latter, in the molten state, with an oxygenated boron compound.
- This treatment effectively removes the sulphur but introduces boron into the alloy.
- the latter is then treated, in a molten condition, with an oxide of manganese, particularly manganese dioxide.
- the boron may be removed to such an extent that it is below the point of accurate analytical determination.
- the result is the preparation of a substantially sulphur-free manganese alloy. In those cases where I boron is not a deleterious constituent of the alloy,
- the present invention enables the production of such alloys simultaneously with the efiective reduction or substantial elimination of sulphur therefrom.
- the oxygenated boron compounds which I employ for the sulphur removal treatment may be selected from a group which includes B203, boric acids, and salts, particularly alkali metal salts, of boric acids such as sodium and potassium metaborates and tetraborates. Of particular utility is sodium tetraborate or borax.
- the sulphur is removed in the form' of a gas, namely, sulphur dioxide.
- the reaction of the sulphur-containing manganese alloy with the oxygenated boron compound is not a surface reaction but the oxygenated boron compound appears to disperse or dissolve in the molten manganese alloy and is apparently in equilibrium with the dispersed or dissolved manganese or other sulphide present in 30 the manganese alloy.
- a substantial, though minor, amount of oxygenated boron compound must be added in some cases to obtain efiective desulphurization. It should be understood that I do not wish to be limited by 35 what the exact mechanism of the reaction may be since the inventionis predicated upon discoveries and results entirely independently of theoretical considerations.
- Erample I pounds of an alloy, comprising 20% 50 nickel, 30% copper and 50% ofelectrolytic manganese containing 0.25% sulphur (the sulphur content based on the alloy as a whole being 0.125%), are melted in a high frequency induction furnace at a temperature between 1300 de- 66 grees C. and 1400 degrees C. To the molten alloy, maintained at the indicated temperature, 8 pounds of borax are added. The stirring which ls produced by the high frequency current is allowed to proceed for 15 to 20 minutes. The borax is then removed as completely as possible from the melt.
- the manganese alloy containing several tenths of one percent of boron, which is produced in part, (a) hereinabove, is mixed, in the molten state, at a temperature of about 1500 degrees C. with 2 pounds of manganese dioxide, the mass being maintained at a temperature of 1500 degrees C. to 1550 degrees C. for between 5 and 15 minutes.
- the manganese oxide slag is then removed and the metal cast into ingots.
- the resulting manganese alloy contains .005% sulphur and .002% boron.
- Example II 100 pounds of an alloy, comprising 15% chromium, 48% iron and 37% electrolytic manga'nese containing 0.28% sulphur (the sulphur content based on the alloy as a whole being about 0.10%), are melted in a high frequency induction furnace at a temperature between 1600 degrees C. and 1650 degrees C. To the molten alloy, maintained at such temperature, 10 pounds of borax are added. The reaction is allowed to proceed for 10 to 20 minutes. The borax is then removed as completely as possible from the melt.
- the manganese alloy, containing several tenths of one percent of boron, which is produced in part (a) of this example, is mixed, in the molten state, at a temperature of about 1600 degrees 0., with 2 pounds of manganese dioxide, the mass being maintained at a temperature of 1600 degrees C. to 1650 degrees C. for between 10 and 20 minutes.
- the manganese oxide slag 40 is then removed and the metal cast into ingots.
- the resulting manganese alloy contains .005% sulphur and .002% boron.
- Example III 100 pounds of an alloy, comprising 10% copper and electrolytic manganese containing 0.24% sulphur (the sulphur content based on the alloy as a whole being about 0.21%), are melted as described in the previous examples at a temperature between 1400 degrees C. and 1450 degrees C. To the molten alloy, maintained at the indicated temperature, 10 pounds of borax are added and the reaction is allowed to proceed for from 10 to 20 minutes. The borax is then removed as completely as possible from the melt.
- the alloys may contain one or more of the elements nickel, copper, iron, carbon, zinc, vanadium, chromium, tungsten, molybdenum, tin, aluminum, beryllium. silver, magnesium, titanium and/or other elements in varying amounts, some from a fraction of one percent to several percent and others as high as about 70%.
- the melting of the manganese alloys is preferably carried out in a highly dense alumina crucible although magnesia crucibles may be used in certain cases. If it is desired to avoid the introduction of silicon into the manganese alloy, crucibles containing silica or silicates should be avoided or, in general, the melt should not be exposed in any way to contact with silica or silicates.
- the proportions of oxygenated boron compounds and oxides of manganese are subject to relatively Wide variations.
- the proportions utilized depend, among other things, on the amount of sulphur present and the amount of boron introduced into the manganese alloy, it being understood that the smaller the percentage of sul- I phur and boron the less oxygenated boron derivatives and oxides of manganese, respectively, will be required.
- from 5% to 10% of borax or the like and from 1% to to 4% of a manganese oxide, based on the weight of the manganese alloy will be suflicient to achieve the desired results.
- the temperature at which the manganese alloys and borax or the like and the oxides of manganese, respectively, are mixed is variable. It should not be so high as to cause undesired volatilization. About 1300 degrees C. to 1600 degrees C. represents a preferred working range, although, of course, the temperature employed will depend upon the nature of the manganese alloy and the nature of the oxygenated boron compound or oxide of manganese, as the case may be. In general, a satisfactory range is from 50 degrees C. to degrees C. above the melting point of the manganese alloy.
- the method of substantially reducing the sulphur content of a manganese alloy containing relatively high proportion of manganese which comprises contacting said alloy, in molten condition, with an oxygenated boron compound for a period of time suflicient to efi'ect the desired removal of thesulphur, whereby boron is introduced into the manganese alloy, and then mixing the resulting manganese alloy, in molten con- 7 tion, with an alkali metal salt of boric acid tor a a of time sufficient to effect the desired removal of the boron.
- the method of substantially reducing th sulphur content of a manganese alloy containing the same which comprises contacting said alloy, in molten condition, with from about to about of an oxygenated boron compound for a period of time sufficient to efiect the desired removal of the sulphur, whereby boron is introduced intorthe manganese alloy, and then.
- the method of substantially reducing the sulphur content of a manganese alloy containing at least 30% electrolytic manganese which comprises agitating said-manganese alloy, at a temperature about-50 degrees C. ormore above its melting point, with borax for a period of time sufiicient to e'fiect the desired removal of the sulphur.
- Themethod of-substantially reducing the boron content of a manganese alloy containing at least 30%'manganese which comprises mixing said manganese alloy, in molten condition, with manganese dioxide at a temperature between about 1300 degrees C. and 1500 degrees C. for a period of time suflicient to effect the desired removal of the boron.
- the method of reducing the sulphur content of manganese alloys containing at least 30% electrolyticmanganese from approximately 0.2% or more to approximately 0.02% or less which comprisesmelting said manganese alloys and mixing the same with borax at a temperature of from about 1300 degrees C. to 1500 degrees C.
- a method of producing a substantially sulphur-free manganese alloy from an alloy prepared from electrolytic manganesasaid alloy initially containing at least 0.05% sulphur which comprises agitating said manganese alloy, in a molten condition, with an oxygenated boron compound for a period of time suflicient to effect the desired removal of the sulphur.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
Patented Nov. 12, 1940 UNITED STATES PATENT OFFICE TREATMENT OF MANGANESE ALLOYS No Drawing. Application February 20, 1939, Serial No. 257,455
14 Claims.
This invention relates to the treatment of manganese alloys and is particularly concerned with the removal of sulphur therefrom in order to provide alloys essentially free of sulphur.
The presence of sulphur in manganese alloys and manganese base alloys is most likely to occur by virtue of the employment of electrolytic manga-nese as a constituent of such alloys. Electrolytic manganese, as prepared in accordance with.
ing or fabricating operations impossible as well as deleteriously aifecting various properties and characteristics of said alloys. While, in many instances, it is of advantage to remove the sulphur from the electrolytic manganese prior to alloying the manganese with such other elements as may comprise the alloys, there are occasions when it may be preferable initially to form the manganese alloy from the electrolytic manganese containing the aforementioned amounts of sulphur and then to treat the resulting alloy ,to effect desulphurization.
It will be clear that if electrolytic manganese containing 0.3% sulphur is employed in an alloy containing say 40% of manganese, the sulphur content of the finished alloy will be 0.12% assuming that sulphur has not been introduced into the alloy from any other source. If, however, the manganese content of the alloy is say 90%, then the sulphur content of the finished alloy would be 0.27%. In the usual case,.-the sulphur content of the alloys should be reduced to not substantially in excess of 0;02% and should preferably be substantially less than that or in other words of the order of a few thousandths of a percent.
In accordance with my present invention, the sulphur, however it may have been introduced into the manganese alloys, is effectively removed in a simple and inexpensive manner.
In general, the removal of the sulphur from the manganese alloys containing the same is efiected by mixing the latter, in the molten state, with an oxygenated boron compound. This treatment effectively removes the sulphur but introduces boron into the alloy. The latter is then treated, in a molten condition, with an oxide of manganese, particularly manganese dioxide. In this manner, the boron may be removed to such an extent that it is below the point of accurate analytical determination. The result is the preparation of a substantially sulphur-free manganese alloy. In those cases where I boron is not a deleterious constituent of the alloy,
it may be permitted to remain in the alloy and the subsequent step of treatment with manganese oxides may be eliminated. Indeed, in certain alloys, the presence of small amounts of boron 1 is highly desirable. The present invention enables the production of such alloys simultaneously with the efiective reduction or substantial elimination of sulphur therefrom.
The oxygenated boron compounds which I employ for the sulphur removal treatment may be selected from a group which includes B203, boric acids, and salts, particularly alkali metal salts, of boric acids such as sodium and potassium metaborates and tetraborates. Of particular utility is sodium tetraborate or borax. The sulphur is removed in the form' of a gas, namely, sulphur dioxide.
The reaction of the sulphur-containing manganese alloy with the oxygenated boron compound is not a surface reaction but the oxygenated boron compound appears to disperse or dissolve in the molten manganese alloy and is apparently in equilibrium with the dispersed or dissolved manganese or other sulphide present in 30 the manganese alloy. As a result, a substantial, though minor, amount of oxygenated boron compound must be added in some cases to obtain efiective desulphurization. It should be understood that I do not wish to be limited by 35 what the exact mechanism of the reaction may be since the inventionis predicated upon discoveries and results entirely independently of theoretical considerations.
The following examples are illustrative of my 40 invention, although it will be appreciated that they are subject to variations with respect to temperatures, times of treatment and character of manganese alloys being treated without departing from the spirit of the invention and the 4.5 novel teachings herein as defined in the appended claims.
Erample I (a) pounds of an alloy, comprising 20% 50 nickel, 30% copper and 50% ofelectrolytic manganese containing 0.25% sulphur (the sulphur content based on the alloy as a whole being 0.125%), are melted in a high frequency induction furnace at a temperature between 1300 de- 66 grees C. and 1400 degrees C. To the molten alloy, maintained at the indicated temperature, 8 pounds of borax are added. The stirring which ls produced by the high frequency current is allowed to proceed for 15 to 20 minutes. The borax is then removed as completely as possible from the melt.
(b) The manganese alloy, containing several tenths of one percent of boron, which is produced in part, (a) hereinabove, is mixed, in the molten state, at a temperature of about 1500 degrees C. with 2 pounds of manganese dioxide, the mass being maintained at a temperature of 1500 degrees C. to 1550 degrees C. for between 5 and 15 minutes. The manganese oxide slag is then removed and the metal cast into ingots. On analysis, the resulting manganese alloy contains .005% sulphur and .002% boron.
Example II (a) 100 pounds of an alloy, comprising 15% chromium, 48% iron and 37% electrolytic manga'nese containing 0.28% sulphur (the sulphur content based on the alloy as a whole being about 0.10%), are melted in a high frequency induction furnace at a temperature between 1600 degrees C. and 1650 degrees C. To the molten alloy, maintained at such temperature, 10 pounds of borax are added. The reaction is allowed to proceed for 10 to 20 minutes. The borax is then removed as completely as possible from the melt.
. (b) The manganese alloy, containing several tenths of one percent of boron, which is produced in part (a) of this example, is mixed, in the molten state, at a temperature of about 1600 degrees 0., with 2 pounds of manganese dioxide, the mass being maintained at a temperature of 1600 degrees C. to 1650 degrees C. for between 10 and 20 minutes. The manganese oxide slag 40 is then removed and the metal cast into ingots.
.On analysis, the resulting manganese alloy contains .005% sulphur and .002% boron.
Example III (a) 100 pounds of an alloy, comprising 10% copper and electrolytic manganese containing 0.24% sulphur (the sulphur content based on the alloy as a whole being about 0.21%), are melted as described in the previous examples at a temperature between 1400 degrees C. and 1450 degrees C. To the molten alloy, maintained at the indicated temperature, 10 pounds of borax are added and the reaction is allowed to proceed for from 10 to 20 minutes. The borax is then removed as completely as possible from the melt.
(b) The manganese alloy, containing several tenths of one percent of boron, which in produced in part (a) of this example, is mixed, in the molten state, at a temperature of about 1450 degrees C. with 5 pounds of manganese oxide, the mass being maintained at a temperature of 1450 degrees C. to 1500 degrees C. for between 10 and 20 minutes. The manganese oxide slag is then removed and the metal cast into ingots. On analysis, the resulting manganese alloy contains .005% sulphur and .009% boron.
While the practice of the invention is illustrated in the above examples with respect to certain alloys, it is of utility in connection with the treatment of all manganese-base alloys, particularly those having a manganese content in excess of 30%. The alloys may contain one or more of the elements nickel, copper, iron, carbon, zinc, vanadium, chromium, tungsten, molybdenum, tin, aluminum, beryllium. silver, magnesium, titanium and/or other elements in varying amounts, some from a fraction of one percent to several percent and others as high as about 70%.
The melting of the manganese alloys is preferably carried out in a highly dense alumina crucible although magnesia crucibles may be used in certain cases. If it is desired to avoid the introduction of silicon into the manganese alloy, crucibles containing silica or silicates should be avoided or, in general, the melt should not be exposed in any way to contact with silica or silicates.
The proportions of oxygenated boron compounds and oxides of manganese are subject to relatively Wide variations. The proportions utilized depend, among other things, on the amount of sulphur present and the amount of boron introduced into the manganese alloy, it being understood that the smaller the percentage of sul- I phur and boron the less oxygenated boron derivatives and oxides of manganese, respectively, will be required. In the average case, from 5% to 10% of borax or the like and from 1% to to 4% of a manganese oxide, based on the weight of the manganese alloy, will be suflicient to achieve the desired results.
The temperature at which the manganese alloys and borax or the like and the oxides of manganese, respectively, are mixed is variable. It should not be so high as to cause undesired volatilization. About 1300 degrees C. to 1600 degrees C. represents a preferred working range, although, of course, the temperature employed will depend upon the nature of the manganese alloy and the nature of the oxygenated boron compound or oxide of manganese, as the case may be. In general, a satisfactory range is from 50 degrees C. to degrees C. above the melting point of the manganese alloy.
It is sometimes advantageous, in carrying out the step of removing the boron, to mix the oxide of manganese with a small amount of a fluxing material such as sodium carbonate, calcium carbonate or calcium fluoride. In general, however, good results are obtained without resorting to such practice.
My copending application, Serial No. 250,377, filed January 11, 1939, discloses and claims the use of oxygenated boron compounds for the desulphurization of electrolytic manganese, while my copending applications, Serial No. 257,456, filed February 20, 1939, and Serial No. 257,457, filed February 20, 1939, relate to the treatment of manganese and manganese alloys, respectively, by means of acidic oxides, of which class of substances, boric acid is a member.
What I claim as new and desire to protect by Letters P-atent of the United States is:
1. The method of substantially reducing the sulphur content of a manganese alloy containing relatively high proportion of manganese, which comprises contacting said alloy, in molten condition, with an oxygenated boron compound for a period of time suflicient to efi'ect the desired removal of thesulphur, whereby boron is introduced into the manganese alloy, and then mixing the resulting manganese alloy, in molten con- 7 tion, with an alkali metal salt of boric acid tor a a of time suficient to effect the desired removal of the boron.
3. The method of substantially reducing the sulphur content of a manganese alloy containing at least 30% manganese and simultaneously said manganese alloy, in molten condition, with an oxide of manganese for a period of time sufficient to efiect the desired removal of the boron. 6. The method of reducing the boron-content of a manganese alloy from approximately 0.1% I
or more to approximately 0.02% or less which comprises mixing said manganese alloy, in molten condition, with manganese dioxide for a period of time sufficient to efiect the desired removal of the boron.
'7. The method of substantially reducing th sulphur content of a manganese alloy containing the same which comprises contacting said alloy, in molten condition, with from about to about of an oxygenated boron compound for a period of time sufficient to efiect the desired removal of the sulphur, whereby boron is introduced intorthe manganese alloy, and then.
mixing the resulting manganese alloy, in molten condition, with from about 1% to 4% of an oxide of manganese for a periodof time sufficient to effect the desired removal of the boron. 8. The method of substantially reducing the sulphur content of a manganese alloy containing at least 30% of electrolytic manganese which comprises contacting said manganese alloy, in
molten condition, with borax for a period of time suflicient to effect the desired removal of the sulphur, whereby boron is introduced into the man ganese alloy, and then mixing the resulting manganese alloy, in molten condition, with manganese dioxide for a period of time sufiicient to effect the desired removal of the boron.
9. The method of substantially reducing the sulphur content of a manganese alloy containing at least 30% electrolytic manganese which comprises agitating said-manganese alloy, at a temperature about-50 degrees C. ormore above its melting point, with borax for a period of time sufiicient to e'fiect the desired removal of the sulphur.
10. Themethod of-substantially reducing the boron content of a manganese alloy containing at least 30%'manganese which comprises mixing said manganese alloy, in molten condition, with manganese dioxide at a temperature between about 1300 degrees C. and 1500 degrees C. for a period of time suflicient to effect the desired removal of the boron.
11.- The method of reducing the boron content of manganese alloys from approximately 0.1% or more to approximately 0.02% or less which com-.
agitating said manganese alloys, in a molten condition, with an alkali metal'salt of boric acid for a period of time suflicient to efiect the desired removal of the sulphur.
13. The method of reducing the sulphur content of manganese alloys containing at least 30% electrolyticmanganese from approximately 0.2% or more to approximately 0.02% or less which comprisesmelting said manganese alloys and mixing the same with borax at a temperature of from about 1300 degrees C. to 1500 degrees C.
14. In a method of producing a substantially sulphur-free manganese alloy from an alloy prepared from electrolytic manganesasaid alloy initially containing at least 0.05% sulphur, which comprises agitating said manganese alloy, in a molten condition, with an oxygenated boron compound for a period of time suflicient to effect the desired removal of the sulphur.
C. TRAVIS ANDERSON.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US257455A US2221624A (en) | 1939-02-20 | 1939-02-20 | Treatment of manganese alloys |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US257455A US2221624A (en) | 1939-02-20 | 1939-02-20 | Treatment of manganese alloys |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2221624A true US2221624A (en) | 1940-11-12 |
Family
ID=22976378
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US257455A Expired - Lifetime US2221624A (en) | 1939-02-20 | 1939-02-20 | Treatment of manganese alloys |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2221624A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2454322A (en) * | 1946-04-17 | 1948-11-23 | Westinghouse Electric Corp | Manufacture of molybdenum |
| EP0067634A3 (en) * | 1981-06-12 | 1983-02-16 | Allegheny Ludlum Steel Corporation | Method of melting an alloy in an induction furnace |
-
1939
- 1939-02-20 US US257455A patent/US2221624A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2454322A (en) * | 1946-04-17 | 1948-11-23 | Westinghouse Electric Corp | Manufacture of molybdenum |
| EP0067634A3 (en) * | 1981-06-12 | 1983-02-16 | Allegheny Ludlum Steel Corporation | Method of melting an alloy in an induction furnace |
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