US1856592A - Silicothermic smelting process and charge therefor - Google Patents

Silicothermic smelting process and charge therefor Download PDF

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US1856592A
US1856592A US479420A US47942030A US1856592A US 1856592 A US1856592 A US 1856592A US 479420 A US479420 A US 479420A US 47942030 A US47942030 A US 47942030A US 1856592 A US1856592 A US 1856592A
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manganese
tungsten
silicon
charge
silicothermic
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US479420A
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William C Read
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ELECTRO METALLURG CO
ELECTRO METALLURGICAL Co
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ELECTRO METALLURG CO
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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B5/00General methods of reducing to metals
    • C22B5/02Dry methods smelting of sulfides or formation of mattes
    • C22B5/04Dry methods smelting of sulfides or formation of mattes by aluminium, other metals or silicon
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C7/00Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B5/00General methods of reducing to metals
    • C22B5/02Dry methods smelting of sulfides or formation of mattes
    • C22B5/06Dry methods smelting of sulfides or formation of mattes by carbides or the like

Definitions

  • Ferrotungsten and ferromolybdenum are usually made directly from ore-concentrates containing tungstates or molybdates, or the corresponding trioxides- These compounds can be reduced silicothermically, that is to say, when they are suitably mixed with.silicon or silicon alloys, with additional substances as explained below, a reaction initiated in the mixture will propagate itself throughout the charge without the further application of heat from extraneous sources.
  • the alkali base tends to volatilize at the high temperature of the silicothermic reduction, and in so doing it absorbs heat.
  • Detrimental proportions of nitrogen may be introduced into the metal by the use of'a nitrate accelerator.
  • the cost of the nitrate is an important item; and when it is stored and handled in large quantities,
  • the present invention is a process for silicothermically smelting the metals of a group which include tungsten and molybdenum.
  • the principal novelty of the invention resides in the use of the higher oxides of manganese as the'accelerator, and of measures whereby to prevent undue contamination of the recovered metal with manganese.
  • the iron appears to be reduced in at least two stages:
  • Ferromolybdenum was made from the following charge Parts Commercial molybdic oxide 2000 Manganese ore 500 Hematite ore 500 Ferrosilicon 59% Si 1090 Steel scrap 30 Metal Slag Mo 78.08% MnO 13.30% Si 1.15% FeO; 22.20% Mn 0.44%. Balance largely SiO The slags produced by my process contain considerable proportions of manganese, which can of course be recovered.
  • a silico-thermic smelting charge comprising as essential components an oxygencontaining compound of a tungsten-group meta-l, manganese oxide material containing loosely bound oxygen, iron oxide material, and silicon; the quantity of manganese oxide material being sufiicient to promote a vigorous self-propagating reaction, and the quantity of silicon being so proportioned with respect to the reducible oxides present that such reaction will produce a low-manganese ferro alloy of the tungsten-group metal.
  • a silico-thermicsmelting charge comprising as essential components an oxygencontaining compound of a tungsten-group metal, pyrolusite, iron oxide material, and silicon; the quantity of pyrolusite material being suflicient to promote a vigorous selfpropagating reaction, and the quantity of silicon being so proportioned with respect to the reducible oxides present that such reaction will produce a low-manganese ferro alloy of the tungsten group metal.
  • a silico-thermic smelting charge comprising as essential components an oxygencontaining compound of a tungsten-group metal, manganese oxide material containing loosely bound oxygen, iron oxide material, and ferro silicon; the quantity of manganese oxide material being sufficient to promote a vigorous self-propagating reaction, and the quantity of silicon being so proportioned with respect to the reducible oxides present that such reaction will produce a low manganese ferro alloy of the tungsten-group metal.
  • a silico-thermic smelting charge comprising as essential components an oxygencontaining compound of tungsten, pyrolusite, iron oxide material, and silicon; the quantity of pyrolusite being suffi-cient to promote a. Vigorous self-propagating reaction, and the quantity of silicon is so proportioned with respect to the reducible oxides present that such reaction will produce a low-manganese ferro tungsten.

Description

Patented May 3, 1932 metallic product.
STATES rast r smear oaeiea WILLIAM C. READ, OF SCARSDALE, NEW YORK, ASSIGNOR TO ELECTRO METALLURGICAL COMPANY, A CORPORATION OF WEST VIRGINIA SILICOTHERMIC SMELTING- IPROCESS AND CHARGE THEREFOR No Drawing.
Ferrotungsten and ferromolybdenum are usually made directly from ore-concentrates containing tungstates or molybdates, or the corresponding trioxides- These compounds can be reduced silicothermically, that is to say, when they are suitably mixed with.silicon or silicon alloys, with additional substances as explained below, a reaction initiated in the mixture will propagate itself throughout the charge without the further application of heat from extraneous sources.
In the silicothermic smelting of" tungsten and molybdenum, it is necessary, or at least expedient, to add to the charge an excess of silicon over the quantity required to reduce the tungsten or molybdenum, and to incorporate with'the charge an energetic oxidizer or accelerator to react with this excess of silicon, thereby developing additional heat to insure a complete reaction and a reguline Sodium nitrate has heretofore been proposed for the accelerator, but the use of this compound involves several difiiculties. It normally carries an objectionable proportion of water, and since it is quite fusible, and easily decomposed by heat, it is difficult to dry. The alkali base tends to volatilize at the high temperature of the silicothermic reduction, and in so doing it absorbs heat. Detrimental proportions of nitrogen may be introduced into the metal by the use of'a nitrate accelerator. The cost of the nitrate is an important item; and when it is stored and handled in large quantities,
the nitrate adds to the fire risk, and may possibly bring about explosions. Other available oxidizing agents are subject to the objections noted, or to others still more serious. I
The present invention is a process for silicothermically smelting the metals of a group which include tungsten and molybdenum. The principal novelty of the invention resides in the use of the higher oxides of manganese as the'accelerator, and of measures whereby to prevent undue contamination of the recovered metal with manganese.
I prefer to use, for the accelerator, an or high in manganese dioxide, but any of the manganese oxides containing a higher pro- Application filed September 2, 1930. Serial No. 479,420.
The last named reduction is an undesirable one since it contaminates the recovered metal wlth manganese. In attempting to adjust the proportion of silicon precisely, so as to efiect the desired reduction while preventin reduct1on-of manganese to metal, I have ha but little success, the usual result being incomplete reduction of the tungsten or molybdenum, or excessive reduction of manganese to metal, or both. I have overcome the difiiculty by using more silicon than is necessary to reduce the tungsten or molybdenum, and
to reduce the manganese oxides to MnO,
and oxidizing the excess of silicon with an 1ron oxide such as ore or mill-scale, thereby protectingthe MnO from reduction. Like the manganese, the iron appears to be reduced in at least two stages:
(1) 2MnO Si= SiO 2MnO (2) 2MnQ Si= SiO 2Mn (3) 2Fe O Si= SiO +4FeO (4) 2FeO+Si=SiO2+2Fe As between reactions (1) and (3), the former probably is preferential, but little or no manganese appears to be reduced to metallic form so long as a considerableproportion of FeO is present, the latter being reduced instead. When an excess of iron oxide is provided, the proportion of silicon in the charge may vary over a considerable range with no other undesirable result than to change the iron content of the alloy produced,an inconsequential matter as compared with an incomplete recovery of the tungsten or molybdenum, or a product rendered unsalabl'e by a high manganese content.
i The following examples are typical: I. A chargewas prepared by thoroughly mixing the following components, all ground 'to pass a No. 100 screen.
e Silicon metal, 97% Si The charge was ignited in a steel shell lined with refractory material. The reactlon was complete in eleven minutes, the slag and metal being fluid, and well separated. The following analytical results are of interest:
Meta] Slag W 81.21% M110 27.07% Si 0.98% SiO 50.72% Mn 0.43% FeO 13.07%
II. Ferromolybdenum was made from the following charge Parts Commercial molybdic oxide 2000 Manganese ore 500 Hematite ore 500 Ferrosilicon 59% Si 1090 Steel scrap 30 Metal Slag Mo 78.08% MnO 13.30% Si 1.15% FeO; 22.20% Mn 0.44%. Balance largely SiO The slags produced by my process contain considerable proportions of manganese, which can of course be recovered.
Falling with tungsten and molybdenum 1n the periodic classification of the elements is the metal chromium. As compared with tungsten and molybdenum, chromium is very diflicult to reduce silicothermically, and I have not as yet 'been able economically to produce chromium or ferrochrome by the method described herein. It is possible, however, to mix a suitable compound of ChI'OIIllllIIl with a reducible compound of tungsten or molybdenum, and then to reduce the mixture by the method which has been described, producing, for example, an alloy of iron, tungsten and chromium free from detrimental proportions of manganese. Accordingly, I
regard the invention as being applicable generally to the metals of the tungsten group.
.In the appended claims that part of the oxygen in the accelerator which is in excess of the quantity corresponding to MnO is referred to as loosely-bound oxygen.
I claim:
1. A silico-thermic smelting charge comprising as essential components an oxygencontaining compound of a tungsten-group meta-l, manganese oxide material containing loosely bound oxygen, iron oxide material, and silicon; the quantity of manganese oxide material being sufiicient to promote a vigorous self-propagating reaction, and the quantity of silicon being so proportioned with respect to the reducible oxides present that such reaction will produce a low-manganese ferro alloy of the tungsten-group metal.
2. A silico-thermicsmelting charge comprising as essential components an oxygencontaining compound of a tungsten-group metal, pyrolusite, iron oxide material, and silicon; the quantity of pyrolusite material being suflicient to promote a vigorous selfpropagating reaction, and the quantity of silicon being so proportioned with respect to the reducible oxides present that such reaction will produce a low-manganese ferro alloy of the tungsten group metal.
3. A silico-thermic smelting charge comprising as essential components an oxygencontaining compound of a tungsten-group metal, manganese oxide material containing loosely bound oxygen, iron oxide material, and ferro silicon; the quantity of manganese oxide material being sufficient to promote a vigorous self-propagating reaction, and the quantity of silicon being so proportioned with respect to the reducible oxides present that such reaction will produce a low manganese ferro alloy of the tungsten-group metal.
4. A silico-thermic smelting charge comprising as essential components an oxygencontaining compound of tungsten, pyrolusite, iron oxide material, and silicon; the quantity of pyrolusite being suffi-cient to promote a. Vigorous self-propagating reaction, and the quantity of silicon is so proportioned with respect to the reducible oxides present that such reaction will produce a low-manganese ferro tungsten. a
In testimony whereof, I atlix my signature.
- WILLIAM C. READ.
US479420A 1930-09-02 1930-09-02 Silicothermic smelting process and charge therefor Expired - Lifetime US1856592A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2834667A (en) * 1954-11-10 1958-05-13 Dominion Magnesium Ltd Method of thermally reducing titanium oxide

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2834667A (en) * 1954-11-10 1958-05-13 Dominion Magnesium Ltd Method of thermally reducing titanium oxide

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