US338722A - Half to henet m - Google Patents

Half to henet m Download PDF

Info

Publication number
US338722A
US338722A US338722DA US338722A US 338722 A US338722 A US 338722A US 338722D A US338722D A US 338722DA US 338722 A US338722 A US 338722A
Authority
US
United States
Prior art keywords
chamber
refining
cones
molten metal
metal
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
Publication date
Application granted granted Critical
Publication of US338722A publication Critical patent/US338722A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00Making metallic powder or suspensions thereof
    • B22F9/02Making metallic powder or suspensions thereof using physical processes
    • B22F9/06Making metallic powder or suspensions thereof using physical processes starting from liquid material
    • B22F9/08Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying
    • B22F9/082Making metallic powder or suspensions thereof using physical processes starting from liquid material by casting, e.g. through sieves or in water, by atomising or spraying atomising using a fluid

Definitions

  • FIG. 1 is a plan View of a plant and sec tional view of the decarburizingchamber for treating the molten metal as it comes from the blast-furnace.
  • Fig. 2 is avertical section of a portion of the blast-furnace and of the chambers for treating the molten metal-viz., an upper or desiliconizing and decarburizing chambers and a lower or recarburizing chamber.
  • Fig. 1 is a plan View of a plant and sec tional view of the decarburizingchamber for treating the molten metal as it comes from the blast-furnace.
  • Fig. 2 is avertical section of a portion of the blast-furnace and of the chambers for treating the molten metal-viz., an upper or desiliconizing and decarburizing chambers and a lower or recarburizing chamber.
  • Fig. 1 is a plan View of a plant and sec tional view of the decarburizingchamber for treating the
  • FIG. 3 is a similar section of a single chamber adapted to serve both purposes.
  • Figs. 4., 5, 6, 7, 8, 9, 10, 11, and 12 are detaitsectional views of revolving cones for spraying or whirling the molten metal, the pillars for supporting said cones, and means for causing a circulation of water for cooling the cones, pillars, and refining-chambers.
  • My present invention has for its object the provision of means whereby the molten metal directly from the blast-furnace may be desiliconized, decarburized, refined, and converted by a continuous process which will avoid the remelting of the metal and the attendant loss and labor incident to the methods now com-
  • the main feature of the invention consists in the construction of a closed chamber which receives the molten metal, and within which are arranged a series of re- 7 volving disks or cones which whirl the metal into showers or spray, into and through which air, gases, and basic or detergent substances are forced for the desiliconization, decarburization and refining of the metal.
  • the minor features embrace the means by which the disks or cones are rotated, the cones and chamber cooled, the air, gas, and basic material introduced and the molten metal transferred from chamber to chamber, all as will hereinafter more fully appear.
  • A indicates a blast-furnace in which the ore is charged and smeltedin the usual manner. If asingle blast-furnace, A, is used, it may be placed directly over the retiu ing-chamber and its hearth a open directly into the chamber, as shown in Fig. 2, while if a eontinuously-operating plant is desired and several blast-furnaces are employed forsmelting the ore they may be arranged in a circle around the refining-chamber with interposed hot-blast ovens B, as shown in Fig.
  • l and one gutter or runner, a, may lead from the furnace to the refiningchamber, and another gutter or runner, a, may lead in the opposite direction (see Fig. 3) to a suitable sand floor orpig-molds. lVith such an arrangement or plant the manufacturer may produce the ordinary pig or refined metal at will.
  • C indicates the refining-chamber, which may have two compartments, one, C, in which the molten metal is desiliconized, decarburized, and refined by the air-blasts, &c., and another, (J, in which it is recarburized, (see Fig. 2;) or it may have a single chamber adapted to both purposes, (see Fig. 3,) as will hereinafter appear.
  • the refining-chamber C may be constructed in any suitable manner, preferably by employing the metallic shell or casing 0, covered above by a fire-brick arch, and so inclosed by exterior walls, a, as to form a waterspace or water-jacket, 0 for the circulation of water entering by pipes c.
  • the circulation of the water may be maintained by a hydrostatic column--elevated reservoirsby a pump, or in any suitable manner.
  • the interior of the refining and converting chambers G (or shell 0) is provided with a lining, a, of any of the well-known refractory materialssuch as gannister, mixtures of fire-clay, lime, silica, and asbestusformed into paste with petroleumheat, so as to form a smooth, hard, non-conductingrefractory lining, such as is required in this class of apparatus.
  • a of any of the well-known refractory materials such as gannister, mixtures of fire-clay, lime, silica, and asbestusformed into paste with petroleumheat, so as to form a smooth, hard, non-conductingrefractory lining, such as is required in this class of apparatus.
  • this charging hole or holes may connect with'the stack A by a gutter, or be located directly under the stack, as herein speci- Moreover, this port or opening d may be closed either by a separate stopper or by one of the revolving disks or cones of the refining-chamber.
  • One or more valved flues, e are also provided in the upper part of the refining-chamber to control and carry off the gases from the refining-chamber O, and these fines for the waste gases may lead to any point where it is desirable to utilize said gases.
  • M indicates man-holes for gaining ad mission to the chamber for repairs, &c.
  • the refining and converting chambers are erected or formed a series of pillars or posts, f, in which are journa'led shafts g, surmounted by cones or disks h.
  • the preferable arrangement of these pillars and cones is that shown in the drawingsthat is to say, a central pillar and cone (which may also serve as a stopper for the charging-port d) and surrounding pillars and cones at a lower level. and in operation it is also preferable to revolve the central cone or disk in reverse direction to the lower surrounding disks or cones, as there,- by the molten metal is better broken up or whirled and sprayed.
  • These pillars or posts f are also hollow for the circulation of water,
  • pipes 2' are arranged within the same so as to discharge at the upper end, (see details, Figs. 4, 5, 6,) and the water may be forced into and through said pipes 21 by hydrostatic pressure, (or a pump, as before specified) and escaping from theopen upper end of the pipe will drop back again through the pillars, thus'protectingthem f rom the intense heat.
  • the shafts g carrying the cones h.
  • these cones h may be simple disks or cones of fire-clay or other refractory material, with ribbed or corrugated faces to swirl the molten metal. They may, however, .be constructed as shown.-that is to say, the cone h may be a hollow chamber communicating with its shaft 9, and a circulation of water may 7 be maintained therethrough by meansof a central water-pipe and hydrostatic; pressure, (see detail, Fig. 11,) by means of an Archimedean screw, (see details, Figs.
  • the shafts g extend through the bottomof refining and converting chambers into a lower or subterranean chamber, D,'wherein is located the mechanism for rotating the shafts and disks, which may consist of bevel-gearing k on the shafts grand bevel driving-gear l on suitable powershafts, m. 7
  • these cones or swirling disks h may be used as stoppers for the charging-openings d, in which case'they would require to be raised and lowered, to accomplish whichthe disk or cone-shaft g is set to move endwise through its bearings and through the carriage s, hereinafter described, and is provided with a rack, n, at its lower end, which gears with a power-pinion, o.
  • each shaft is provided with a collar, 1), which supports it upon a carriage, 8, (see- Fig. 12,) through which theshaft passes loosely, and
  • the carriage s is provided with anti-friction rollers r, resting upon aplate, t, securediu theenlarged base of the pillar or post f.
  • This carriage s carries the entire weight of the shaft and its adjuncts, so that the beveled wheels below are relieved of all burden.
  • the bottom or hearth of the refining and converting chambers is so constructed that the metal will collect at the :lowest point at the tapping-holes w, and at a suitable distance above the tapping-holes'slag ports 3 are provided.
  • a series of valved air and gas pipes project into the refining-ch'amher through the walls thereof, at intervals all around the same, and at different heights or levels, so as to subject the molten spray to cross-jets of air and gas, which assist in the tooagitation as well as serve to refine the metal.
  • the air and gas pipes may, if desired, unite in a single tuyere or nozzle; but for the purposes of illustration I have shown these pipes arranged in clusters consisting of a central airjet, X, and a series of surrounding gas-jets,V, and as a means ofintroducing pulverized basic material into the molten mass in the refining-chamber I have shown hoppers i or funnels Z, connected with the air-pipes by valved pipes a.
  • the air and gas tuyeres w and 1) might also be placed in alternate rows, or the gas exclusively might be blowninto the chamber in the upper part or in the lower part, as best suited, and the air alternately with the gas in the lower or upper part of the chamber, as under some circumstances it will: be, found desirable to subject the molten metal to air only or to gas only in one part or in the whole of the chamber.
  • the upper chamber may be provided only with the airjets X and the basic receptacles Z.
  • the basic receptacles Z may be omitted in the chamber C, but where the decarburizing, purifying, refining, and converting processes are to be simultaneously carried on in a single chamber the construction adopted is that shown in the lower chamber, Fig. 2, or in the single chamber 0, Fig. 3.
  • the blast-furnace may be elevated on a stone foundation to such height as will permit the refining-chamber O to belocated above ground, the gear-chamberD being in such case the only subterranean part of the apparatus.
  • T (see Fig. 1,) may inclose the plant, and in order to utilize the waste gases from the convertingchamber 0 the waste-gas fines e may be made to deliver into the hot-blast ovens B.
  • the devices being of substantially the character hereinbefore described will be employed as follows: From the hearth or crucible of blast-furnace A the fluid metal is tapped into and through port (Z upon the revolving cone h, which whirls it off into sheet or spray form in the upper part of refining-chamber C, where it is met and traversed by cross-currents of air and gas charged with basic material, as in Fig. 3, and falling upon the lower row of cones is again broken into spray and whirled, being met by further cross-currents of air, gas, 850.
  • the molten metal thus purified, refined, and converted collects in the bottom of the refiningchamber 0, where it can be further treated by blasts through pipes d, if desired, and whence itis drawn through tap 10 into ingot-molds or into other chambers for any further treatment that may be deemed desirable.
  • a refining-chamber having a hollow watercooled pillar, and a rotating cone or disk shaft j ournaled in the pillar, substantially as and for the purposes specified.

Landscapes

  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)

Description

(No Model.) 2 Sheets-Sheet 1.
. E. P. FALOONNET.
APPARATUS FOR THE MANUFACTURE OF IRON AND STEEL. N0. 338 722.
u. PKTERs Pnmoumu n hnr. Wishinglon, 0.0.
(No Model.) 2 Sheets-Sheet 2.
E. F. FALGONNET.
APPARATUS FOR THE MANUFAGTURE OF IRON AND STEEL.
No. 338,722. Patented Mgr. 30, 1886.
r r I I III/III/II/IIIIIIIIIIlllIIII]IIIIIIIIIIIIIIIIIIIIIIII/IM' I 5 1 N. PETERS. mouu w. Washington. ma
monly practiced.
NITED STATES PATENT Orrica.
EUGENE F. FALCONNET, OF NASHVILLE, TENNESSEE, ASSIGNOR OF ONE- HALF TO HENRY M. PIERCE, OF SAME PLACE.
APPARATUS FOR THE MANUFACTURE OF IRON AND STEEL.
SPECIPICATIONforming part of Letters Patent NO. 338,722, dated March 30, 1886.
(No model.)
To all whom it may concern.-
Be it known that I, EUGENE F. FALOONNET, of Nashville, in the county of Davidson and State of Tennessee, have invented a certain new and useful Improvement in Apparatus for hereby declare the following to be a full,clear, and exact description of the same, reference being had to the accompanying drawings, in which- Figure 1 is a plan View of a plant and sec tional view of the decarburizingchamber for treating the molten metal as it comes from the blast-furnace. Fig. 2 is avertical section of a portion of the blast-furnace and of the chambers for treating the molten metal-viz., an upper or desiliconizing and decarburizing chambers and a lower or recarburizing chamber. Fig. 3 is a similar section of a single chamber adapted to serve both purposes. Figs. 4., 5, 6, 7, 8, 9, 10, 11, and 12 are detaitsectional views of revolving cones for spraying or whirling the molten metal, the pillars for supporting said cones, and means for causing a circulation of water for cooling the cones, pillars, and refining-chambers.
Like letters refer to like parts wherever they occur.
My present invention has for its object the provision of means whereby the molten metal directly from the blast-furnace may be desiliconized, decarburized, refined, and converted by a continuous process which will avoid the remelting of the metal and the attendant loss and labor incident to the methods now com- To this end the main feature of the invention consists in the construction of a closed chamber which receives the molten metal, and within which are arranged a series of re- 7 volving disks or cones which whirl the metal into showers or spray, into and through which air, gases, and basic or detergent substances are forced for the desiliconization, decarburization and refining of the metal. The minor features embrace the means by which the disks or cones are rotated, the cones and chamber cooled, the air, gas, and basic material introduced and the molten metal transferred from chamber to chamber, all as will hereinafter more fully appear.
I will now proceed to describe my invention more fully, so that others skilled in the art to which it appertains may apply the same. the Manufacture of Iron and Steel; and I In the drawings, A indicates a blast-furnace in which the ore is charged and smeltedin the usual manner. If asingle blast-furnace, A, is used, it may be placed directly over the retiu ing-chamber and its hearth a open directly into the chamber, as shown in Fig. 2, while if a eontinuously-operating plant is desired and several blast-furnaces are employed forsmelting the ore they may be arranged in a circle around the refining-chamber with interposed hot-blast ovens B, as shown in Fig. l, and one gutter or runner, a, may lead from the furnace to the refiningchamber, and another gutter or runner, a, may lead in the opposite direction (see Fig. 3) to a suitable sand floor orpig-molds. lVith such an arrangement or plant the manufacturer may produce the ordinary pig or refined metal at will.
C indicates the refining-chamber, which may have two compartments, one, C, in which the molten metal is desiliconized, decarburized, and refined by the air-blasts, &c., and another, (J, in which it is recarburized, (see Fig. 2;) or it may have a single chamber adapted to both purposes, (see Fig. 3,) as will hereinafter appear. The same general construction exists in both cases, and described in detail is as follows: The refining-chamber C may be constructed in any suitable manner, preferably by employing the metallic shell or casing 0, covered above by a fire-brick arch, and so inclosed by exterior walls, a, as to form a waterspace or water-jacket, 0 for the circulation of water entering by pipes c. The circulation of the water may be maintained by a hydrostatic column--elevated reservoirsby a pump, or in any suitable manner. The interior of the refining and converting chambers G (or shell 0) is provided with a lining, a, of any of the well-known refractory materialssuch as gannister, mixtures of fire-clay, lime, silica, and asbestusformed into paste with petroleumheat, so as to form a smooth, hard, non-conductingrefractory lining, such as is required in this class of apparatus.
In the crown or top of the refining and 0011- ve'rting chamber is one or more charging-holes, d, for the introduction of the molten metal, andthis charging hole or holes may connect with'the stack A by a gutter, or be located directly under the stack, as herein speci- Moreover, this port or opening d may be closed either by a separate stopper or by one of the revolving disks or cones of the refining-chamber. One or more valved flues, e, are also provided in the upper part of the refining-chamber to control and carry off the gases from the refining-chamber O, and these fines for the waste gases may lead to any point where it is desirable to utilize said gases.
M indicates man-holes for gaining ad mission to the chamber for repairs, &c. I
\Vithin the refining and converting chambers are erected or formed a series of pillars or posts, f, in which are journa'led shafts g, surmounted by cones or disks h. The preferable arrangement of these pillars and cones is that shown in the drawingsthat is to say, a central pillar and cone (which may also serve as a stopper for the charging-port d) and surrounding pillars and cones at a lower level. and in operation it is also preferable to revolve the central cone or disk in reverse direction to the lower surrounding disks or cones, as there,- by the molten metal is better broken up or whirled and sprayed. These pillars or posts f are also hollow for the circulation of water,
and may be formed of a metallic shell roughe. ened and covered'with a refractory covering of the character before specified; or they may be formed or molded from plastic refractory material and burned, as in the manufacture of fire-brick and like articles. In either case they should be provided with brasses or boxes f above for the shafting of the disks or cones h.
In order to maintain a circulation of water in these posts or pillars, pipes 2' are arranged within the same so as to discharge at the upper end, (see details, Figs. 4, 5, 6,) and the water may be forced into and through said pipes 21 by hydrostatic pressure, (or a pump, as before specified) and escaping from theopen upper end of the pipe will drop back again through the pillars, thus'protectingthem f rom the intense heat.
Journaled in the pillars f. are the shafts g, carrying the cones h. As these cones h can be readily renewed, they may be simple disks or cones of fire-clay or other refractory material, with ribbed or corrugated faces to swirl the molten metal. They may, however, .be constructed as shown.-that is to say, the cone h may be a hollow chamber communicating with its shaft 9, and a circulation of water may 7 be maintained therethrough by meansof a central water-pipe and hydrostatic; pressure, (see detail, Fig. 11,) by means of an Archimedean screw, (see details, Figs. 7, 8-, 9, and l.O,) with supply and waste tanks, or in any other well-known ways of obtaining a circulation of water under similar circumstances. The shafts g extend through the bottomof refining and converting chambers into a lower or subterranean chamber, D,'wherein is located the mechanism for rotating the shafts and disks, which may consist of bevel-gearing k on the shafts grand bevel driving-gear l on suitable powershafts, m. 7
As before specified, these cones or swirling disks h may be used as stoppers for the charging-openings d, in which case'they would require to be raised and lowered, to accomplish whichthe disk or cone-shaft g is set to move endwise through its bearings and through the carriage s, hereinafter described, and is provided with a rack, n, at its lower end, which gears with a power-pinion, o. I In order to support the cone-shafts g and permit of their being readily rotated, each shaft is provided with a collar, 1), which supports it upon a carriage, 8, (see- Fig. 12,) through which theshaft passes loosely, and
the carriage s is provided with anti-friction rollers r, resting upon aplate, t, securediu theenlarged base of the pillar or post f.
This carriage s carries the entire weight of the shaft and its adjuncts, so that the beveled wheels below are relieved of all burden.
Having described the mechanism by which the molten metal is swirled or sprayed, I will next describe the means for injecting the air, gas, and basic material in the treatment of the molten spray. The bottom or hearth of the refining and converting chambers is so constructed that the metal will collect at the :lowest point at the tapping-holes w, and at a suitable distance above the tapping-holes'slag ports 3 are provided. A series of valved air and gas pipesproject into the refining-ch'amher through the walls thereof, at intervals all around the same, and at different heights or levels, so as to subject the molten spray to cross-jets of air and gas, which assist in the tooagitation as well as serve to refine the metal.
For this purpose the air and gas pipes may, if desired, unite in a single tuyere or nozzle; but for the purposes of illustration I have shown these pipes arranged in clusters consisting of a central airjet, X, and a series of surrounding gas-jets,V, and as a means ofintroducing pulverized basic material into the molten mass in the refining-chamber I have shown hoppers i or funnels Z, connected with the air-pipes by valved pipes a. The air and gas tuyeres w and 1) might also be placed in alternate rows, or the gas exclusively might be blowninto the chamber in the upper part or in the lower part, as best suited, and the air alternately with the gas in the lower or upper part of the chamber, as under some circumstances it will: be, found desirable to subject the molten metal to air only or to gas only in one part or in the whole of the chamber.
. \Vhere it is preferred to first decarburize,
desiliconize, and refine the metal in one chamber and then recarburize and further treat it in a second chamber, the upper chamber (see C, Fig. 2) may be provided only with the airjets X and the basic receptacles Z. The basic receptacles Z may be omitted in the chamber C, but where the decarburizing, purifying, refining, and converting processes are to be simultaneously carried on in a single chamber the construction adopted is that shown in the lower chamber, Fig. 2, or in the single chamber 0, Fig. 3.
As a matter of preferred construction the blast-furnace may be elevated on a stone foundation to such height as will permit the refining-chamber O to belocated above ground, the gear-chamberD being in such case the only subterranean part of the apparatus.
As a matter of convenience a track, T, (see Fig. 1,) may inclose the plant, and in order to utilize the waste gases from the convertingchamber 0 the waste-gas fines e may be made to deliver into the hot-blast ovens B.
The devices being of substantially the character hereinbefore described will be employed as follows: From the hearth or crucible of blast-furnace A the fluid metal is tapped into and through port (Z upon the revolving cone h, which whirls it off into sheet or spray form in the upper part of refining-chamber C, where it is met and traversed by cross-currents of air and gas charged with basic material, as in Fig. 3, and falling upon the lower row of cones is again broken into spray and whirled, being met by further cross-currents of air, gas, 850. The molten metal thus purified, refined, and converted collects in the bottom of the refiningchamber 0, where it can be further treated by blasts through pipes d, if desired, and whence itis drawn through tap 10 into ingot-molds or into other chambers for any further treatment that may be deemed desirable.
\Vhere it is proposed to decarburize, desiliconize, and treat with basic materials prior to recarburizing and refining by carbonic oxide, hydrocarbon, and other gases, and the upper chamber, 0, Fig. 2, is used, the molten metal, when whirled and sprayed by the disk or cone h, is subjected only to airblasts charged with pulverized basic substances such as iron oxide, ground magnesium, limestone, &c.which will suffice to desiliconize, decarburize, desulphurize, and dephosphorize the molten metal, after which it is drawn into chamber 0 and treated with gas, or air and gas, for conversion.
I do not herein claim the process of dephosphorizing, desulphurizing, and refining metal by subjecting it while in the form of molten spray to the action of air currents charged with fine basic substances for refining and converting the metal, as the same forms the subject-matter of case Serial No. 165,880, filed of even date herewith.
I am aware that in the production of solid castings a centrifugal pan, disk, or table surrounded by a channel for the reception of the molten metal and arranged in a closed or Vacuum chamber having an outlet for gases and an inlet for air and gas for the preliminary heating of the apparatus has been devised to free the metal of occluded gases, and do not herein claim such devices, as they are not adapted to refine the metal, which must be subjected to jets of air,or air and gas,charged with basic material; but,
Having thus described my invention, what I claim, and desire to secure by Letters Patent, 1S-
1. In apparatus for treating molten metal, the combination, with a refiningchamber provided with a series of tuyeres, of one or more revoluble spraying disks or cones arranged in said chamber, substantially as and for the purposes specified.
2. In apparatus for treating molten metal, the combination, with the refining-chamber, of one or more revoluble spraying disks or cones, and a series of tuyeres arranged at intervals and at different levels around the refining-chamber, substantially as and for the purposes specified.
3. In apparatus for treating molten metal, the combination, with the refining'chamber, of one or more revoluble spraying-disks, a series of tuyeres arranged around and delivering into the refining-chamber, and basic receptacles connected with and delivering into the blast pipes or tuyeres, substantially as and for the purposes specified.
4. In apparatus for refining metal, the combination, with the refining-chamber, of two or more revoluble spraying cones or disks arranged on different levels within the refiningchamber, substantially as and for the purposes specified.
5. In apparatus for refining metal, the combination, with the refining-chamber, of two or more revoluble spraying disks or cones arranged on different levels within the refiningchamber and geared to revolve in reverse direction, substantially as and for the purposes specified.
6. In apparatus for refining and converting metal, the combination, with the refiningchamber, of one or more revoluble spraying cones or disks, and a series of air and gas tuyeres arranged around and delivering into the refining and converting chamber at intervals above the bottom thereof, substantially as and for the purposes specified.
7. In apparatus for treating molten metal, a refining-chamber having a hollow watercooled pillar, and a rotating cone or disk shaft j ournaled in the pillar, substantially as and for the purposes specified.
8. In apparatus for treating molten metal, the combination of the water-jacketed refining-chamber provided with water-cooled pillars, and cone or disk shafts j ournaled in said pillars, and the subterranean gear-chamber provided with the gearing for rotating and raising the cone-shafts, substantially as and for the purposes specified.-
9. In apparatus for refining and converting molten metal, the combination of an upper and a lower communicating chamber, each provided with revoluble-spraying cones and ch'an1ber,sf1bstanti'al1yas and for tliepurpose's IO disks, and t-uyeres deliveringthrongh the side specified.
walls of the chambers at different levels, sub- In testimony whereof I affix my signature, stantially as and for the purposes specified. in presence of two witnesses, this 5th day of 10. In an apparatus for refining molten May, 1885. l metal, the combination,with arefining-charnv v EUGENE F. FALOONNET. her having a hollow water-cooled pillar, of a WVitnesses: hollow water-cooled revoluble disk and disk W. D. .TALBOT,
shaft jonrnaled in the pillar of the refining" v GEO. E. PURVIS.
US338722D Half to henet m Expired - Lifetime US338722A (en)

Publications (1)

Publication Number Publication Date
US338722A true US338722A (en) 1886-03-30

Family

ID=2407807

Family Applications (1)

Application Number Title Priority Date Filing Date
US338722D Expired - Lifetime US338722A (en) Half to henet m

Country Status (1)

Country Link
US (1) US338722A (en)

Similar Documents

Publication Publication Date Title
RU2431682C2 (en) Installation for direct melting
US3194650A (en) Metallurgical melting and refining process
US338722A (en) Half to henet m
US3364009A (en) Method for the production of iron and steel
US1815899A (en) Method for the treatment of iron ore
US502482A (en) August dauber
US2249410A (en) Method and apparatus for reducing ore
US688651A (en) Combined ore roaster and smelter.
US3992194A (en) Method and apparatus for use in the treatment of metals in the liquid state
US2356524A (en) Method of directly producing pig iron and steel
US2690333A (en) Apparatus for smelting oxide ores
US3503736A (en) Direct iron and steelmaking process
USRE26364E (en) Metallurgical melting amd refining process
US324903A (en) Apparatus for converting iron into steel
US331267A (en) williamson
US414654A (en) District
US2136360A (en) Process for reducing iron in a blast furnace
CN2288182Y (en) Side-bottom-blown blast furnace for smelting iron and steel
US4347079A (en) Method of operating an open-hearth furnace
US1775955A (en) Blast furnace
US511919A (en) Alexandre tropenas
US372912A (en) Gas blast-furnace
US238628A (en) wurtenberger
US3802682A (en) Method for continuously refining pig iron and plant for carrying out such method
US138429A (en) Improvement in combined rotary blast and puddling furnaces for making wrought