|Publication number||US1061256 A|
|Publication date||May 13, 1913|
|Filing date||Nov 28, 1911|
|Priority date||Nov 28, 1911|
|Publication number||US 1061256 A, US 1061256A, US-A-1061256, US1061256 A, US1061256A|
|Inventors||Thomas B Allen, Frank J Tone|
|Original Assignee||Carborundum Co|
|Export Citation||BiBTeX, EndNote, RefMan|
|Referenced by (5), Classifications (2)|
|External Links: USPTO, USPTO Assignment, Espacenet|
' UNITED STATES PATENT OFFICE.
THOMAS B. ALLEN AND FRANK J. TONE, F NIAGARA FALLS, NEW YORK, ASSIGNORS TO THE GARBORUNDUM COMPANY, OF NIAGARA FALLS, NEW YORK, A CORPORA- TION OF PENNSYLVANIA.
MANUFACTURE or SILICON.
1,061,256. No Drawing.
To all whom it may concern:
Be it known that we, THOMAS B. ALLEN and FRANK J. TONE, residents of Niagara Falls, in the county of Niagara and State of New York, have invented a new and useful Improvement in the Manufacture of Silicon, of which the following is a full, clear, and exact description. I
Our invention relates particularly to the manufacture of silicon, its alloys and compounds, in a new and efficient mannerthough our process is applicable to electrical treatment of other ores where there is alarge or considerable loss due to volatilization. a
In the regular manufacture of silicon, its alloys and compounds, it has been found that there is a very considerable waste of material and electrical energy due to the poor recovery of silicon from the furnace charge. The reaction zone of the furnace producin this substance has a positive pressure 0 considerable magnitude and consequently if the furnace charge is of such a nature that the escapev of a large volume of carbon monoxid gas takes place along a few paths, the large volume of carbon monoxid gas carries with it a considerable proportion of the vapors of silicon, silicon monoxid and sili con dioxid. These vapors on coming in contact with the air are transformed into silicon dioxid. In using an electric furnace of the arc type for the manufacture of silicon it is found that the necessary free movement of the electrodes causes a path of weakness in the furnace charge and allows the ready escape of gases along this parting line-or path. As the furnace mixture is in general quite compact, there is no easy path of egress forthe gases except along the electrodes and consequently the carbon monoxid gas formed by reduction escapes almost entirely along these paths. Such paths, therefore, become very highly heated, thus further reducing the possibility of condensation of the silicious vapors.
' great loss of material and electrical energy.
In manufacturing silicon; and by the term silicon as hereafter used, we intend .to
include also its alloys and compounds, it has been found that better results are obtained where thesilicious material and reducing agent are both in a fine state of division and are intimately mixed. This in- Specification of Letters Intent. Application filed November 28 1911. Serial No. 662,950.
Consequently there is a Patented May 13, 1913.
creases the efliciency of the furnace. We have also found that by briqueting an intimate mixture of finely divided carbonaceous and sllicious materials, and then subjecting this briqueted mixture to electrically developed heat in an electric furnace, we can obtain a greatly increased efliciency in furnace practice and also materially decrease the loss of silica from the furnace charge, and the silicon monoxid and silicon, after the reduction has started to take Place.
We will now describe in detail a preferred method of carrying out our invention for the .production of metallic silicon.
We take 70 parts by weight of pure silica sand and 30 parts by weight of petroleum coke, the materials being preferably in a fine state of division, forexample, 12 mesh and finer. These materials are then mixed with about 7 per cent. by Weight of hard pitch, which serves as the binder for the briquets. The mixture is then passed.
through a heater of any well known type and then placed in a hot mixer so that the pitch softens and is thoroughly mixed with the furnace charge. This hot mixture. is then fed into a briqueting machine of any well known type and is formed into briquets. The briquets are discharged from the machine and are then preferably cooled, for example, by spraying with water and are then transported to the furnace. Diflerent shapes of briquets may be obtained by changing the shape of the die used in the briqueting machine, butwe have found that the spherical shape gives the greatest amount of interstitial space and consequently is best adapted for our purpose. We prefer to use brlquets 1%" in diameter. The briquets thus obtained may be charged into any desirable ty e of furnace; and for this purpose we pre er to use a furnace of the arc type such as shown in United States Patent No. 921183, granted on May 11, 1909, to Frank J. Tone (one of the inventors herein). This furnace is operated in the usual manner and owing to the briqueting of the finely divided materials, we find thatthe efficiency of the furnace is greatly increased and the loss of material reduced, by reason of the discharge of carbon monoxid quite uniformly throughout the entire mass of the charge. Instead of discharging the carbon monoxid gas along the line of the electrode with little condensation of the silicon containingvapors carried along thereby, the carbon monoxid The method above described of disposing the briqueted charge so that it will .act as a condensin medium for the volatile reduction pro ucts may be applied with ad.- vantage to the reduction of many other ores where there is a considerable loss byvolatilization; for instance to the reduction of the ores of aluminum, boron and manganese, and other changes may be made in the materials em loyed and in the steps of the process without departing from our invention.
1. In the manufacture of silicon, the step cons sting in subjecting briquets containing silicious and carbonaceous material to the direct heat of an electric arc. v
2. In the manufacture of silicon, the step consisting in briqueting a finely divided mixture of silicious and carbonaceous material and subjecting the briquets to the direct heat of an' electric arc.-
3. In the manufacture of silicon, the
method consisting of subjecting a briqueted mixture of finely divided silicious and car bonaceous materials to the direct heat of an electric arc.
1. In the manufacture of silicon, the steps.
consisting in 'briqueting. a mixture of silicious ore and carbon, charging the same-into the reaction zone of an electric furnace, subjecting it to the direct heat of an electric arc, and causing the outgoing gases to permeate and pre-heat the charge.
5. In the manufacture of silicon, the steps consisting of charging an electric furnace with a briqueted mixture and disposing said charge so that on subjecting it to electrically developed heat it will act as a condensing medium for the volatile reduction products carried by the outgoing gases.
6. In a process-employing electrically developed heat, the step consisting of electrically heating a briqueted mixture and using said briqueted charge as a condensing medium for volatile reduction products.
7. In the reduction of materials subject to large losses by volatilization, the method consisting in charging an electric furnace with a briqueted mixture thereof, disposing said charge so that it will act as a condensing medium for the volatile products c ar= ried by the outgoing gases,'and subjectmg said charge to electrically developed heat.
In testimony whereof, we have hereunto set our hands.
THOS. B. ALLEN.
FRANK J. TONE- Witnesses as to T. B. Allen:
F. W. HOLLMANN, O. H. GREENWOOD.
Witnesses as to F. J. Tone: BENJ. S. GALLAND, A. P. FRANoHoT.
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|US2773745 *||Jul 20, 1954||Dec 11, 1956||Du Pont||Process for the production of pure silicon in a coarse crystalline form|
|US2979449 *||Dec 5, 1958||Apr 11, 1961||Sheer Korman Associates||Carbothermic reduction of metal oxides|
|US3806586 *||Jun 14, 1971||Apr 23, 1974||Kema Nord Ab||Process for producing higher yields of silicon|
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