US943599A - Method of and apparatus for returning flue-dust to blast-furnaces. - Google Patents

Method of and apparatus for returning flue-dust to blast-furnaces. Download PDF

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US943599A
US943599A US48931709A US1909489317A US943599A US 943599 A US943599 A US 943599A US 48931709 A US48931709 A US 48931709A US 1909489317 A US1909489317 A US 1909489317A US 943599 A US943599 A US 943599A
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dust
blast
flue
hopper
furnace
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William B Hubbard
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    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S75/00Specialized metallurgical processes, compositions for use therein, consolidated metal powder compositions, and loose metal particulate mixtures
    • Y10S75/961Treating flue dust to obtain metal other than by consolidation

Description

. W. B. HUBBARD. METHOD OF AND APPARATUS FOR RETURNING FLUE DUST T0 BLAST FURNACES:
Patented Dec. 14,1909.
WILLIAM B. HUBBARD, OF CHICAGO, ILLINOIS.
METHOD OF AND APPARATUS FOR RETURNING FLUE-DUST TO BLAST-FURNACES.
Specification of Letters Patent.
Patented Dec. 14, 1909.
Application filcd April 12, 1909. Serial No. 489,317.
To all whom it may concern: 7
Be it known that I, I/VILLIAM B. HUBBARD, a citizen of the United States, residing at Chicago, in the county of Cook and State of Illinois, have invented certain new and useful Improvements in Methods of and Apparatus for Returning Flue-Dust to Blastl urnaces, of which the following is a specification.
This invention relates to the art of blast furnaces for the reduction of iron and other ores, and has for its main object to effect a pronounced economy in the operation of such furnaces through the saving of what has hitherto constituted a waste product.
On account of the increased used of the Mesabi or soft ores in the present state of the art of smelting iron ores, the amount of flue-dust carried away from the blast furnaces by the gases has increased accordingly. In some instances this waste product amounts to as much as 3 per cent. of the total material charged or pericerft. of the total ore charged. It is a well known fact that the gaseous products discharged from a blast furnace employed in the smelting of iron ore carry with them as flue-dust a percentage of fine iron ore, coke dust, etc., the amount of metallic iron thus carried off being in some instances as high as 54 per cent. of the total matter passing ofi with the gases. This waste product, or, as it is known in the art, flue-dust, is driven out of the furnace by the blast, instead of being smelted in the furnace, and represents a waste product the metallic contents of which would become valuable were it recovered; and, so far as I am aware, this has never been successfully accomplished, although attempts have been made to effect its return to and reduction in the blast furnace. Owing to its light and finely divided physical constitution, it cannot be successfully introduced at the top of the furnace and caused to settle therein with the materials as charged against the force of the blast pressure which is introduced at the twyers in the lower part of the blast furnace. The solution of this problem presented by my present invention involves the return of this product to the lower portion of the furnace through the twyer openings by the agency of the hot blast that is led into the interior of the furnace through the twyer openings. In the broadest aspect of my invention this product may be introduced into the presence of the hot blast by any means or in any manner; but my preferred method of returning the flue-dust consists in subjecting a body of the latter to the pressure of the hot blast, feeding the flue-dust by its own gravity on its way' to the furnace. I preferably effect the introduction of the finedust into the hotblast main which leads to the bustle-pipe, from which a series of twyer stocks and blow-pipes lead into the side walls of the furnace; but it should be understood that the particular point of introduction of the flue-dust into the presence of the hot blast is immaterial under the broadest aspect of the invention.
One means by which I am enabled to effectuate the purposes of the invention, and which I have selected for the sake of illustrating the latter, consists essentially of a flue-dust hopper communicating with the hot blast main or other conducting pipe of the hot blast, and a pipe also communicating with said hot blast main or other conducting pipe of the hot blast, or other source of pneumatic pressure, and leading into said fluedust hopper so as to create in the latter a pressure substantially equal to that obtaining in-the pipe or main through which the hot blast is traveling. Preferably communication of said hopper and the said pipe with the hot blast main or other source of pressure is controlled by valves, in order that the feed of the flue-dust into the presence of the hot blast may be regulated to the most eflicient point.
My invention will be readily understood when considered in connection with the accompanying drawing, in which I have shown one simple form of apparatus for the carrying out thereof, and in which,
Figure l is a side elevation, partly broken out, of my improved apparatus shown as applied to the hot blast main of a blast furnace, a portion of this latter, as also of the hot blast main and bustle-pipe being shown in vertical section. Fig. 2 is a detail top plan view of a graduated valve that may be employed to control the feed from the finedust hopper into the hot blast main. Fig. 3 is a longitudinal section on the line 3-3 of Fig. 2.
Referring to the drawin 5 designates the lower portion of the wal of an ordinary blast furnace employed for the reduction of iron ores, surrounding which is the usual blowers and stoves (not shown). coupled to a hollow boss 10 on the hot blastmain 9 is the lower end of a flue-dust hopper 1.1,"the latter having a cover 12 equipped with a suitable opening indicated at 13 for charging the hopper with flue-dust. ably coupled to a similar hollow boss 14 at another place on the hot blast main, is a pipe 15 which passes'through thecover 12 -of the flue-dust hopper and preferably ex tends to a point near the lower end of the latter, as shown by dotted lines. The pipe 15 is equipped with a suitable valve indicated at 16, while the bottom of the hopper llis also equipped with a suitable valve for controlling the flow of the flue-dust thence into the hot blast main; one form of such a valve being shown in detail in Figs. 2 and 3 and comprising a sliding valve-bar 17 formed in its upper-surface with a series of shallow pockets l8, l9 and 20, of the same area as and adapted to register with, the opening in the bottom of the'hopper, and said pockets having formed through their bottom walls valve- ports 21, 22 and 23 of varying sizes. The valve-bar 17 may also be equipped .at one end with a hook or handle 24 .for its convenient manipulation.
In the operation of the apparatus,lfluedust having been put into the hopper 11 and the opening 13 tightly closed, the valves 16 and 17 are then opened, whereby an equilibrium of pressures is established within .the' hopper 11, the pressure in the main opposing the flow of the flue-dust into the latter being neutralized by the same pressure introduced into the hopper through the pipe 15. The result of this 1s that the fluedust flows, under the influence of its own gravity, in a steady and continuous stream (the slze of which may be regulated by the valve 17 from the hopper into the current of air or hot blast flowing through the main 9, with which blast it becomes thoroughly commingled and distributed throughout the bustle-pipe 6, whence it passes through the twyer-stocks and twyer-openings 8 into the lower hottest portion of the furnace where a temperature considerably above the melting point of iron is constantly maintained; so
, that the metallic content of said flue-dust is reduced upon or soon after its'introduction into the furnace, and is thus added to the molten metal in the hearth of the furnace.
While the pressure-equalizing pipe 15 ma be led into the hopper at any point thereo yet I have determined by experiment that the best and most satisfactory results are secured by leading the said pipe to a point at 'or near the bottom of the hopper and of Suitthe charge of flue-dust therein, as is indicated in the drawing. Lateral holes may also be introduced at various points in that portion of the equalizing pipe 15 lying within the hopper, as indicated at 15. This may be done in order to secure a better equalization of pressure in the flue-dust hopper than-. where the discharge is'wholly through the lower open end of said ipe. While I have shown these means for e ecting the introduc- 7 tion of the flue-dust into the presence of the air supplied to the hotblast mainnear the unction of the latter with the bustle-pipe, and
in practice prefer to apply it at that point, yet it will-be manifest that the flue-dust in- 30 troducing means might be applied elsewhere without .any' variation in or departure from the principle of operation involved. Also, while I have shown the neutralizing pressure admitted to thefl'ue-dust hopper as drawn from .5 the hot air blast, it will be evident that this pressure might be drawn from an independent source so long as it is substantially equal to the pressure of the hot blast. Obviously, also, the structural and mechanicaldetails of the apparatus may be varied asdesired or found convenient without involving any departure from the invention or sacrificing any of the advantages thereof Hence, it should be understood that the invention is by no means limited to the apparatus illustrated and described in the carrying out of the same, except to the extent clearly indicated in specific claims.
I claim: 4
1. The herein described method of effecting the return of flue-dust to a blast furnace, which consists in introducing said flue-dust into the presence of the hot blast on its way I to the twyer openings of the furnace, sub stantially as described.
2. The herein described method of effecting the return of flue-dust to a blast. furnace, which consists in subjecting a confined body of flue-dust to a pressure substantially 11 equal to that of the hotblastyand permitting the flue-dust to flow under the influence of gravity into the presence of the latter, substantially as described. x
3. The herein described method of eflecting the return of flue dust to a blast-furnace, whichconsists in introducin into the presenceof a confined body of ue-dust a body of air drawn from. and having substantially the pressure of the hot blast, and permitting the flue-dust to flow under the influence of gravity into the presence of the latter, sub stantially as described.
4. In an apparatus for effecting the return of flue-dust to a blast furnace, the combination with an air-blast conducting pipe leading into the furnace, 'of a flue-dust hopper mounted thereon and communicating therewith, and means for creatingin saidhop er a pressure-substantially equal to that existing in said air-blast conducting pipe, substantially as described.
5. In an apparatus for effecting the return of flue-dust to a blast furnace, the combination with an airblast conducting pipe leading into the furnace, of a flue-dust hopper mounted thereon and communicating at its lower end therewith, and a pipe connecting said air-blast conducting pipe with the interior of said hopper at a point above the communication of the latter with said air-blast conducting pipe, substantially as described.
(3. In an apparatus for effecting the return of flue-dust to a blast furnace, the combination with an air-blast conducting pipe leadinginto the furnace, of a flue-dust hopper mounted thereon and connected at its lower end therewith, means for creating in said hopper a pressure substantially equal to that existing in said air-blast conducting pipe, and a valve in the connection between said hopper and air-blast conducting pipe and controlling the communication therebetween, substantially as described.
7. In an apparatus for effecting the return of flue-dust toa blast furnace, the combination with an air-blast conducting pipe leading into the furnace, of a flue-dust hopper mounted thereon and connected at its lower end therewith, means for creating in said hopper a pressure substantially equal to that existing in said air-blast conducting pipe, and a graduated valve in the connection between said hopper and air-blast conducting pipe and controlling the .flow of flue-dust from the former into the latter.
substantially as described.
8. In an apparatus for eifecting the return of flue-dust to a blast furnace, the combination with an air-blast conducting pipe leading into the furnace, of a flue-dust hopper mounted thereon and communicating at its lower end therewith, and a. pipe leading from said air-blast conducting pipe through the cover of said hopper and terminating at a point near the bottom of the latter, substantially as described.
9."In an apparatus for effecting the return of flue-dust to a blast furnace, the combination with the hotblast main of the furnace, of a hopper mounted on and communicating at its lower end with said hot-blast main, a valve controlling said communication, a pressure-neutralizing pipe leading from said hot-blast main into said hopper and terminating ata point near the bottom of the latter, and a valve in said neutralizing pipe, substantially as described.
In testimony that I claim the foregoing as my invention, I have hereunto subscribed my name in the presence of two witnesses.
WILLIAM B. HUBBARD.
Witnesses SAMUEL N. Ponn, MA'L'IIE B. Brfrss.
US48931709A 1909-04-12 1909-04-12 Method of and apparatus for returning flue-dust to blast-furnaces. Expired - Lifetime US943599A (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2544697A (en) * 1946-12-31 1951-03-13 Standard Oil Dev Co Blast furnace operation
US2846301A (en) * 1956-08-29 1958-08-05 William E Greenawalt Processes of smelting finely divided metallic ore
US2905523A (en) * 1955-12-19 1959-09-22 Oxy Catalyst Inc Method for the elimination of finely divided carbonaceous material from gas streams
US2938782A (en) * 1956-04-24 1960-05-31 Commw Engineering Corp Method and operation of blast furnaces and metallurgical fuels therefor
US3323904A (en) * 1963-10-07 1967-06-06 Yawata Iron & Steel Co Method of operating a blast furnace
US3454395A (en) * 1966-04-15 1969-07-08 Gerald F H Von Stroh Process for the reduction of iron ore in a cupola-type furnace

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2544697A (en) * 1946-12-31 1951-03-13 Standard Oil Dev Co Blast furnace operation
US2905523A (en) * 1955-12-19 1959-09-22 Oxy Catalyst Inc Method for the elimination of finely divided carbonaceous material from gas streams
US2938782A (en) * 1956-04-24 1960-05-31 Commw Engineering Corp Method and operation of blast furnaces and metallurgical fuels therefor
US2846301A (en) * 1956-08-29 1958-08-05 William E Greenawalt Processes of smelting finely divided metallic ore
US3323904A (en) * 1963-10-07 1967-06-06 Yawata Iron & Steel Co Method of operating a blast furnace
US3454395A (en) * 1966-04-15 1969-07-08 Gerald F H Von Stroh Process for the reduction of iron ore in a cupola-type furnace

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