US120165A - Improvement in furnaces for roasting and smelting ores - Google Patents

Improvement in furnaces for roasting and smelting ores Download PDF

Info

Publication number
US120165A
US120165A US120165DA US120165A US 120165 A US120165 A US 120165A US 120165D A US120165D A US 120165DA US 120165 A US120165 A US 120165A
Authority
US
United States
Prior art keywords
furnace
water
roasting
tank
ore
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 US120165A publication Critical patent/US120165A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B17/00Furnaces of a kind not covered by any preceding group
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B9/00General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
    • C22B9/02Refining by liquating, filtering, centrifuging, distilling, or supersonic wave action including acoustic waves

Definitions

  • My invention consists of certain improvements, too fully explained hereafter to need preliminary description, in roasting and smelting ores, the said improvements having been designed mainly with the View of recovering by condensation the volatile and other constituents of the ore, which in ordinary furnaces are permitted to pass oif through the stack or stacks; of preventing the escape of noxious gases into the surrounding atmosphere; of granulating the molten metal as it is withdrawn from the smelting-furnace; and of preventing the burning out of the roof and other portions of the furnace.
  • FIG l Sheet 1 is a vertical sectional view of a roasting-furn ace with my improvements 5 Fi g. 2, a sectional view of the lower portion of the same on the line 1 2, Fig. 1; Fig. 3, a sectional plan on the line 3 4, Fig. 2; Fig. 4, Sheet 2, a longitudinal vertical section of a smelting-furnace with my improvements; Fig. 5, a transverse sectilon on the line 5 6, Fig. 4 5 and Fig. 6, a sectional p an.
  • A represents an upright roastingfurnace somewhat resembling a cupola in its interior construction.
  • This furnace has at the top a charging-hole, a, covered by an iron plate, al, except when the charge of combined ore and fuel is being introduced; and the furnace has an inclined bottom, b', terminating atits lowest point in a discharge-opening, c, through which the roasted ore is withdrawn, as hereafter described.
  • the sta-ck at the top of the furnace first ascends vertically for a short distance, as shown at d, and is then extended horizontally or slightly inclined downward over awater-vessel, B, as shown at d', the stack being then extended vertically upward from a point directly over the water-vessel to any desired height.
  • the vessel B is to be filled with pure water, which constantly enters it through a pipe, e, an d is as constantly discharged from the top of the vessel at about the point ef.
  • a water-tank, G mounted upon wheels for convenience in moving it about from place to place, is arranged to receive the roasted ore as it is drawn from the furnace through the opening o,
  • the smelting-furnace in which the ore is treated after its removal from the roasting-furnace is illustrated in Sheet 2 ofthe drawing, D representing the body of the furnace, built of or lined with suitable refractory material; c, the ash-pit, f, the grate, g, the fire-chamber; L, the blast pipe, entering the furnace beneath the grate; i, thebridge-wall; j, the basin, into which themolten metal is received; and 7:, the bench upon which the ore and iux is placed, and which inclines downward toward the basin.
  • the basin is a deep semi-cylindrical depression formed within the furnace between the bridge-wall and the bench, and communicating at its opposite ends with two discharge-openings or tapping-holes, l and Z, one for the slag and the other for the molten metal.
  • the roof of the furnace above the fire-place is curved, and inclined downward toward the basin, as shown at m in Fig.
  • This tank is constantly supplied with running water in the same manner as the tank B of the roasting furnace by means of a pipe, r, and the water constantly flows oft' from the tank at the point t after passing beneath partitions s and s. Access can be obtained to the interior of the furnace through openings u u, and to the interior of the horizontal iiue n through openings t and vf for purposes of cleansing, &c.
  • raw ore is, in the rst instance, introduced intoV ically suspended in the heated ascending current of the products of combustion, rise through the vertical and horizontal portions d and d1 of the stack, and pass flnally into the stack proper d2.
  • a considerable'portion of the water in the tank B, over which the heated products ofy combustion are thus caused to pass, will be converted into steam, which will mingle with the said products and separate from the same by condensation the volatile matters and particles held in suspension, which condensed particles will fall back into the water.
  • the water is caused to flow continuously through the vessel in order that those condensed matters which are soluble in water may be at once carried off with the same instead of being permitted to remain and saturate the water, and thus prevent the deposit of pure metals in the latter.
  • lt is important, also, that the water should be constantly changed in order to keep up the supply which is constantly decreased by evaporation, and in order, also. to maintain it in as cool a state as possible so as to effect a more perfect condensation.
  • the roasted ore (at about red heat) is discharged from the opening c at the bottom of the furnace into the water-tank C.
  • This sudden change of temperatureand plunging' into water causes the ore to crumble, and enables the sulphurous acid and some other impurities to be driven off; a decomposition, in other words, taking place, and the impurities being absorbed by the water, While a considerable percentage of oxygen is taken up by the ore.
  • the ore After having been thus treated the ore is dried, and is then mixed with a suitable flux or fluxes and placed upon the bench K of the smelting-furnace, where it is subjected to a most intense heat caused to impinge directly upon it, as before described, by reason of the peculiarly-curved roof m of the front portion of the furnace and descendin g iiue n at the rear end of the same, the products of combustion having no tendency to rise after striking the basin and bench, but passing over the bench and through the mass of ore until the latter is thoroughlymelted and flows down into the basin.
  • This method of directing the heated products of combustion onto the ore also protects the roof of the furnace, and prevents that ra-pid burning out of the same, which is so great an objection in ordinary furnaces.
  • the water-tank F beneath the horizontal flue a and vertical stack p is intended for precisely the same purpose as the tank B of the roastingfurnace, namely, to condense and recover the volatile metals and matters held in suspension by the products of combustion, and also to prevent the escape of noxious gases from the stack into the surrounding atmosphere.
  • This tank has also a supply of water running constantly through it so as to carry off impurities, to prevent undue heating, and to effect a perfect condensation.
  • the lid of the tank can be removed at any time, and the condensed particles raked up and Withdrawn from the bottom of the same without interfering with the draught of the furnace.
  • the slag iswithdrawn from the basin of the furnace through the tapping-hole l, and the molten metal or matt is withdrawn through the hole l and discharged at once into the water-tank This granulating the metal or matt, so that it can, when removed from the tank, be at once treated with the proper chemicals for the purpose of separating the different kinds of metals-the usual necessity of remelting the metal or matt for the purpose of granulating it-being thus avoided.
  • the arrangement, beneath and combination with the outlet-liuc or stack of aroasting or smelting-furnace, of a body of water ilo win g freely and constantly, and over which the gases are caused to pass, all substantially as and for the purpose specified.
  • a smelting-furnace in which an arched or curved roof, m, and descending flue a are combined with and arranged in respect to the basin and bench of the said furnace, substantially as herein described.

Description

UnrTnn STATES PATEN WILLIAM QUANN, OF PHILADELPHIA, PENNSYLVANIA, ASSIGNOR TO HIMSELF, JOHN W. THAOKARA, AND EDWARD L. SPAIN, OF SAME PLACE.
IMPROVEMENT IN FURNACES FOR ROASTENG AND SNIELTING ORES.
Specification forming part of .Letters Patent No. 120,165, dated October 24, 1871.
To all whom it may concern:
Be it known that I, W'ILLIAM QUANN, of Philadelphia, county of Philadelphia, State of Pennsylvania, have invented certain Improvements in Roasting and Smelting Ores, of which the following is a specification:
My invention consists of certain improvements, too fully explained hereafter to need preliminary description, in roasting and smelting ores, the said improvements having been designed mainly with the View of recovering by condensation the volatile and other constituents of the ore, which in ordinary furnaces are permitted to pass oif through the stack or stacks; of preventing the escape of noxious gases into the surrounding atmosphere; of granulating the molten metal as it is withdrawn from the smelting-furnace; and of preventing the burning out of the roof and other portions of the furnace.
Figure l, Sheet 1, is a vertical sectional view of a roasting-furn ace with my improvements 5 Fi g. 2, a sectional view of the lower portion of the same on the line 1 2, Fig. 1; Fig. 3, a sectional plan on the line 3 4, Fig. 2; Fig. 4, Sheet 2, a longitudinal vertical section of a smelting-furnace with my improvements; Fig. 5, a transverse sectilon on the line 5 6, Fig. 4 5 and Fig. 6, a sectional p an.
In Sheet l, A represents an upright roastingfurnace somewhat resembling a cupola in its interior construction. This furnace has at the top a charging-hole, a, covered by an iron plate, al, except when the charge of combined ore and fuel is being introduced; and the furnace has an inclined bottom, b', terminating atits lowest point in a discharge-opening, c, through which the roasted ore is withdrawn, as hereafter described. The sta-ck at the top of the furnace first ascends vertically for a short distance, as shown at d, and is then extended horizontally or slightly inclined downward over awater-vessel, B, as shown at d', the stack being then extended vertically upward from a point directly over the water-vessel to any desired height. The vessel B is to be filled with pure water, which constantly enters it through a pipe, e, an d is as constantly discharged from the top of the vessel at about the point ef. A water-tank, G, mounted upon wheels for convenience in moving it about from place to place, is arranged to receive the roasted ore as it is drawn from the furnace through the opening o,
the object of which will be hereafter described. The smelting-furnace in which the ore is treated after its removal from the roasting-furnace is illustrated in Sheet 2 ofthe drawing, D representing the body of the furnace, built of or lined with suitable refractory material; c, the ash-pit, f, the grate, g, the fire-chamber; L, the blast pipe, entering the furnace beneath the grate; i, thebridge-wall; j, the basin, into which themolten metal is received; and 7:, the bench upon which the ore and iux is placed, and which inclines downward toward the basin. The basin is a deep semi-cylindrical depression formed within the furnace between the bridge-wall and the bench, and communicating at its opposite ends with two discharge-openings or tapping-holes, l and Z, one for the slag and the other for the molten metal. A water-tank, a', Figs. 5 and o', placed beneath the opening from which the inolten metal is discharged so as to receive and at once granulate the latter, as hereafter described. The roof of the furnace above the lire-place is curved, and inclined downward toward the basin, as shown at m in Fig. 4, for the purpose of directing the products of combustion down into the basin and onto the bench beyond the same; and the products of combustion, thus directed in the first instance, are caused to pass over the surface of the bench instead of rising as usual to the roof of the furnace by means of a descending flue, a, at the end of the furnace, this flue anda horizontal passage, n', forming a communication between thefurnace and a vertical stack, p, through which the products of combustion finally escape. The products of combustion in their passage through the horizontal flue n are conveyed over water contained in a tank, F, which is also arranged beneath the vertical stack, and extends outward beyond the latter, where it is provided with a lid, q. This tank is constantly supplied with running water in the same manner as the tank B of the roasting furnace by means of a pipe, r, and the water constantly flows oft' from the tank at the point t after passing beneath partitions s and s. Access can be obtained to the interior of the furnace through openings u u, and to the interior of the horizontal iiue n through openings t and vf for purposes of cleansing, &c.
rIhe ore is submitted to the following treatment in the roasting and smelting-furnaces: The
raw ore is, in the rst instance, introduced intoV ically suspended in the heated ascending current of the products of combustion, rise through the vertical and horizontal portions d and d1 of the stack, and pass flnally into the stack proper d2. A considerable'portion of the water in the tank B, over which the heated products ofy combustion are thus caused to pass, will be converted into steam, which will mingle with the said products and separate from the same by condensation the volatile matters and particles held in suspension, which condensed particles will fall back into the water. This process of condensa tion is continued up through the vertical stack d2, which is situated directly over the water-vessel, so that particles will be constantly disengaged and condensed, and will fall back into the water contained in the said vessel, the consequence being that most of the volatile matters are recovered, while but a small proportion of noxious vapors escape from the top of the stack to taint the surrounding atmosphere. The condensed metals fall to the bottoni of the tank, from which they can be removed from time to time without interfering with or stopping the furnace, as one end of the tank projects outward beyond the flue so as to permit the introduction into the same of proper tools for raking up and withdrawing the condensed particles.
The water, as before mentioned, is caused to flow continuously through the vessel in order that those condensed matters which are soluble in water may be at once carried off with the same instead of being permitted to remain and saturate the water, and thus prevent the deposit of pure metals in the latter. lt is important, also, that the water should be constantly changed in order to keep up the supply which is constantly decreased by evaporation, and in order, also. to maintain it in as cool a state as possible so as to effect a more perfect condensation.
lt should be understood that but a portion of the Volatile metals, and sulphur and other impurities, are disengaged by the roasting process. The remainder have to be disengaged in the subsequent operations, which I will now proceed to describe.
The roasted ore (at about red heat) is discharged from the opening c at the bottom of the furnace into the water-tank C. This sudden change of temperatureand plunging' into water causes the ore to crumble, and enables the sulphurous acid and some other impurities to be driven off; a decomposition, in other words, taking place, and the impurities being absorbed by the water, While a considerable percentage of oxygen is taken up by the ore.
After having been thus treated the ore is dried, and is then mixed with a suitable flux or fluxes and placed upon the bench K of the smelting-furnace, where it is subjected to a most intense heat caused to impinge directly upon it, as before described, by reason of the peculiarly-curved roof m of the front portion of the furnace and descendin g iiue n at the rear end of the same, the products of combustion having no tendency to rise after striking the basin and bench, but passing over the bench and through the mass of ore until the latter is thoroughlymelted and flows down into the basin. This method of directing the heated products of combustion onto the ore also protects the roof of the furnace, and prevents that ra-pid burning out of the same, which is so great an objection in ordinary furnaces.
The water-tank F beneath the horizontal flue a and vertical stack p is intended for precisely the same purpose as the tank B of the roastingfurnace, namely, to condense and recover the volatile metals and matters held in suspension by the products of combustion, and also to prevent the escape of noxious gases from the stack into the surrounding atmosphere. This tank has also a supply of water running constantly through it so as to carry off impurities, to prevent undue heating, and to effect a perfect condensation. The lid of the tank can be removed at any time, and the condensed particles raked up and Withdrawn from the bottom of the same without interfering with the draught of the furnace. The slag iswithdrawn from the basin of the furnace through the tapping-hole l, and the molten metal or matt is withdrawn through the hole l and discharged at once into the water-tank This granulating the metal or matt, so that it can, when removed from the tank, be at once treated with the proper chemicals for the purpose of separating the different kinds of metals-the usual necessity of remelting the metal or matt for the purpose of granulating it-being thus avoided.
I claim as my invention- 1l. The arrangement, beneath and combination with the outlet-liuc or stack of aroasting or smelting-furnace, of a body of water ilo win g freely and constantly, and over which the gases are caused to pass, all substantially as and for the purpose specified.
2. A smelting-furnace in which an arched or curved roof, m, and descending flue a are combined with and arranged in respect to the basin and bench of the said furnace, substantially as herein described.
In testimony whereof I have signed my name to this specification in the presence of two subscribing witnesses.
WILLLAM QUANN.
"Witnesses:
JOHN K. RUPERTUs,
HARRY SMITH.` (99)
US120165D Improvement in furnaces for roasting and smelting ores Expired - Lifetime US120165A (en)

Publications (1)

Publication Number Publication Date
US120165A true US120165A (en) 1871-10-24

Family

ID=2189612

Family Applications (1)

Application Number Title Priority Date Filing Date
US120165D Expired - Lifetime US120165A (en) Improvement in furnaces for roasting and smelting ores

Country Status (1)

Country Link
US (1) US120165A (en)

Similar Documents

Publication Publication Date Title
US120165A (en) Improvement in furnaces for roasting and smelting ores
US792632A (en) Manufacture of salt.
US4073645A (en) Process of smelting sulphidic copper ore concentrates
US596992A (en) Xmethod o of and apparatus for-bgssemerizinq matte
US1817043A (en) Converter smelting
US227710A (en) adams
US782123A (en) Method of matte or pyritic smelting.
US894764A (en) Process of preparing arsenic trioxid.
US156243A (en) Improvement in reducing ores
US515727A (en) Louis robert bonehill
US198283A (en) Improvement in shaft-furnaces for smelting tailings and condensing mercury
US493076A (en) Charles james fatjvel
US207065A (en) Improvement in ore roasting and desulphurizing furnaces
US2207779A (en) Process and apparatus for zinc smelting
US791928A (en) Process of treating ferruginous ore for the manufacture of iron and steel therefrom.
US607497A (en) westman
US298426A (en) Furnace for the manufacture of metals direct from the ore
US106553A (en) Improvement in roasting-furnaces for ores
US236562A (en) George dtteyee
US228965A (en) Rudolf wiester
US406870A (en) Process of smelting ores
US420029A (en) Metallurgical furnace
US696323A (en) Quicksilver-separating and continuous ore-furnace.
US2234473A (en) Metallurgical apparatus
US243850A (en) claek