US116558A - Improvement in smelting iron ores - Google Patents

Improvement in smelting iron ores Download PDF

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US116558A
US116558A US116558DA US116558A US 116558 A US116558 A US 116558A US 116558D A US116558D A US 116558DA US 116558 A US116558 A US 116558A
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kiln
gas
chamber
combustion
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    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B13/00Making spongy iron or liquid steel, by direct processes
    • C21B13/0073Selection or treatment of the reducing gases

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
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  • Metallurgy (AREA)
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  • Manufacture And Refinement Of Metals (AREA)

Description

UNITED STATES PATENT GEEIGE.
IMPROVEMENT lN SMELTING IRON ORES.
Specification forming part of Letters Patent No. 116,558, dated July 4, 1871.
To all whom 'it may concern:
Be it known that I, CHARLES GocERANE, of The Ellowes,7 Upper Gornal, in the county of Stafford, England, have invented an Improved Mode of, and Apparatus, Kiln, or Furnace for, Preparing Iron Ores for Smelting; and do hereby declare that the following description, taken in connection with the accompanying drawing,
hereinafter referred to, forms a full and eXact specification of the same, wherein I have set forth the nature and principles of my said improvement, by which my invention may be distin guished from others of a similar class, together with such parts as I claim and desire to secure by Letters Patent-that is to say:
My invention has reference to the process of deoxidizing iron ores, before introduction into the blast-furnace, by subjecting the same to the action of carbonic-oxide gas; and consists of an improved method, whereby, instead of acting upon cold-iron ore with highly-heated carbonicoXide or blast-furnace gas, as described in the specification to another patent for which I am applying, or instead of simultaneously heating the ore and the carbonic-oxide gas, as is effected to a certain extent in the iblast-furnace, and as has also otherwise been proposed, the iron ore is first heated to the requisite degree in one part of a special furnace or kiln, and then in another part of such kiln is subjected to the action of carbonio-oxide or blast-furnace gas, which has not been specially heated for this purpose.
Various arrangements may be employed for carrying this invention into practice. Thus in one arrangement I introduce the ore into a chamber or kiln, at or near the lower end of which cool carbonio-oxide or blast-furnace gas is made to enter, which gas, after ascending through the lower stratums of the ore, is, in the upper part of the kiln, (constituting a combustion-chamber which may or may not be separated from the lower part or reducing-chamber of the kiln,) brought into contact with jets of atmospheric air, and, in entering into combustion therewith, is caused to heat the ore contained in such combustion-chamber to the requisite degree before it descends into the reducing-chamber of the kiln, where it is acted upon by the carbonio-oxide gas, and
whence it afterwards issues through chutes at the bottom. By this arrangement the heat contained in the ore is utilized by being taken up by the gas on its way to the combustion-chamber, the ore passing away from the kiln in a comparatively cool state, and thus the loss of heat arising in the before-mentioned processes through the passing away of the ore in a highly-heated condition is prevented. In this arrangement a sucient quantity of carbonio-oxide or blast-furnace gas must be introduced into the reducingchamber to afford the requisite surplus of unconverted gas after passing through the ore for producing the necessary heat by combustion with the air in the combustion-chamber. In another arrangement the necessary quantity of combustible gas is introduced directly and separately into the combustion-chamber, and only such a quantity of carbonio-oxide or blast-furnace gas is passed into the reducing-chamber as is requisite for deoxidiziug the ore. The heat of such gas, if any is left after passing from the reducingchamber, may, if desired, be utilized by causing the gas to pass in contact with the pipes or iiues conducting the air or combustible gas, or both, into the combustion-chamber, or the hot gas may be allowed to rise up among the ore in the combustion-chamber.
Having thus set forth the nature of my invention, I will now proceed more particularly to describe the manner in which it is to be performed, for which purpose I shall refer to the accompanying drawing, showing one of the various arrangements of kilns or furnaces by which my invention may be carried into effect.
Figure l on Sheet I shows a vertical section of the kiln. Fig. 2, Sheet I, shows a sectional plan of the same on line X X, Fig. l. Figs. 3 and AL, on SheetII, show, respectively, an enlarged section on line Y Y Fig. 4, and a section on line Z Z, Fig. 3, of one ofthe discharging-boxes.
Similar letters of reference indicate similar parts in each of the figures.
The furnace or kiln consists of a chamber, A,"
of fire-brick, inclosed in an iron casing, which chamber is closed at its upper end by a bell- Valve, B, above which is a closed feeding-hopper, C, for the introduction of the ore, for the construction of which Letters Patent for Great Britain and Ireland have been granted to me, bearing date 21st February, 1868, No. 579. The lower end of the` chamber A is supported by columns I I, and is contracted to a funnel-shape at A', into the center of which rises the passage for carbonio-oxide or blast-furnace gas D, terminating in a conical orifice, D, covered by a conical hood, E, so that the gases passing from the passage D issue into the kiln from under the edge of the hood E. The annular` space formed between the sloping sides A of the chamber A and the surface of the conical orifice D has a number of outlet-apertures, F, connnunicating with the iron discharge-boxes G, fixed by their upper ends in an air-tight manner to and suspended from the ironcasing of the kiln. Between the outlet-apertures F are formed ridges F to prevent the lodging of ore in the spaces between the apertures. The construction and mode of operating the discharge-boxes G will be more readily understood on reference to the enlarged views thereof shown on Sheet II. In order to discharge the reduced ore from the kiln without at the same time allowing atmospheric air to enter the kiln through the dischargeboxes, each box is provided with three sets of slides, Hl H2 H3, of which those H1 serve to cut off the communication between the kiln and the box, while those H2 cut of the communication between the upper part and the lower part of the box, and those H3 close the lower end of the box. By this arrangement, if the slides H1 are opened, (H2 being closed,) a quantity of reduced ore will fall from the kiln into the upper part of box. If, now, the slides Hl are closed an'd those H2 are opened, (H3 being closed,) the ore contained in the upper part of the box will fall into the lower part, and after the slides H2 have been closed, and those H3 are open, the ore is discharged into the trucks or onto the ground. The slides H1 Hl are opened and closed in opposite directions, re-
spectively, by means Vof the lever K, having itsY fulcrum at K, and by means of a pinion, L, in gear with the rack L on the slide, the spindle ofthe pinion being rotated by a grooved pulley, M, fixed on the same, worked by an endless chain, N. The slides H2 are actuated in a direction at right angles to H1 by means of the levers O O working on fulcrums O O fixed to the columns I. The slides H3 are worked by pinions P in gear with racks on the slides, and rotated by means of crank-handles In order to prevent any escape of carbonio-oxide gas at the slides Hl H2 these are made to work backward and forward inside closed casings G1 G2 projecting from the discharge-box G, also, in order to prevent as much as possible the entrance of air into the lower 'part of the discharge-box, when the slides H3 are opened for discharging the reduced ore, carbonicoxide gas may be introduced into such lower space through the aperture G2. Should it be found at any time that the ore does not descend readily into the discharge-boxes from the kihi, stoppered apertures It It are provided, through which prizing-bars may be introduced, and to which access is gained from the gallery S. At some height above the inlet D', for the carbonicoxide gas, side apertures T T are formed round the kiln for the inlet of atmospheric air, or in order to effect the combustion of the unconverted portion of the carbonio-oxide gasrising up from below. The air-holes are capable of being closed by stoppers T', so as to regulate the inlet of air to the exact extent required. Access is gained to the air-holes from the gallery U.
The action of the kiln takes place as follows: The kiln being charged with ore, the lower portion of which may be introdued either in a heated or cool state, and the valveB and hopper() closed, carbonica-oxide gas or blast-furnace gas, or other suitable reducing-gas, is introduced through the passage D into the bottom of the kiln, and in rising up through the heated lower portion of the ore it acts upon and deoxidizes the same more or less completely, at the same time taking up the heat therefrom and becoming itself converted into carbonio-acid gas. The reducing-gas is, however, introduced in such quantity as to be in excess of the amount required for reducing the ore, so that the unconverted portion thereof, in rising up in a heated state to the level of the air-holes T, enters into combustion with the air passing in, and thereby heats the ore in the upper part ofthe kiln to the requisite degree before it is made to descend into the lower part, in order in its turn to be reduced by the incoming carbonic-oxide gas. The deoxidation of the lower portion of the ore having thus been effected it is discharged in a comparatively cool state into the discharging-boxes G, as before described, and fresh ore is introduced into the kiln through the valve B at top. The carbonio-acid and other gases, in rising up through the mass of ore above the air-holes T, impart their heat to the same, and finally escape through the side aperture V into a iiue, in which a draught is produced, either by a chimney or by an exhaust-fan, or by both. Should it be found that the air entering through the apertures T doesY not penetrate sufficientlyY Y through the mass of ore to effect the equable heating of all parts of the same, this may be facilitated by causing it to pass in through perforated radial pipes W, shown in dotted lines in Fig. l, leading from the apertures T to a central annular pipe, W1, connecting all the radial pipes, and supported by means of stays W2.
As before stated, the arrangement of the furnace or kiln may be variously modified for carrying my invention into practice. Thus the upper part or combustion-chamber of the kiln may be separated from the lower part or reducing-chamber, and be furnished with a separate supply of combustible gas for raisingthe ore to the requisite temperature; or one or more heating-chamber or chambers or retorts may be arranged at the top of the kiln and the heated ore be discharged thence into the kiln. Also, the reducing-gas may be made to enter the kiln through several side apertures instead of through one single central passage, and the discharge of the reduced ore may be effected in any other convenient manner, whereby the inlet of the atmospheric air into the lower part ofthe kiln is practically prevented.
Having thus set forth the nature of my invention, and in what manner the same is to be performed, I wish it to be understood that I do not limit myself to the precise means or apparatus for carrying the same into effect, as hereinbefore described, with reference to the accompanying drawing, as these maybevariously modified, as already stated, without departing from the nature of my invention; neither do I claim as part of my invention the various details of construction of apparatus hereinbefore described7 except when used in combination for the purposes of my invention. Also, I am aware that kilns have before been constructed with a central inlet for combustible gases, covered by a conical hood, but for totally diierent purposes, namely, for calcining minerals and other substances-that is to say, for subjecting the sanie to an oxidizing flame; whereas, by my invention, the ore is subjected to the ac tion of reducing-gases, and the introduction of oxidizinggases, as in caleining operations, is carefully avoided; but
Deoxidizing or reducing iron ores .before their introduction into the blast-furnace by first raising the ores to the requisite degree of heat, and
then subjecting the saine to the action ofcar- Witnesses Guns. D. ABEL, J No. BN. MILLARD.
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2993779A (en) * 1958-01-22 1961-07-25 Elektrokemisk As Process of reducing metal oxides
US3202405A (en) * 1962-07-18 1965-08-24 Midland Lime Inc Vertical shaft kiln and method of operation thereof
US20100091844A1 (en) * 2006-03-30 2010-04-15 Byeong Moon Jeon Method and apparatus for decoding/encoding a video signal
US20100104014A1 (en) * 2006-08-25 2010-04-29 Han Suh Koo Method and apparatus for decoding/encoding a video signal

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2993779A (en) * 1958-01-22 1961-07-25 Elektrokemisk As Process of reducing metal oxides
US3202405A (en) * 1962-07-18 1965-08-24 Midland Lime Inc Vertical shaft kiln and method of operation thereof
US20100091844A1 (en) * 2006-03-30 2010-04-15 Byeong Moon Jeon Method and apparatus for decoding/encoding a video signal
US20100104014A1 (en) * 2006-08-25 2010-04-29 Han Suh Koo Method and apparatus for decoding/encoding a video signal

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