US1415183A - Metallurgical apparatus - Google Patents
Metallurgical apparatus Download PDFInfo
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- US1415183A US1415183A US248854A US24885418A US1415183A US 1415183 A US1415183 A US 1415183A US 248854 A US248854 A US 248854A US 24885418 A US24885418 A US 24885418A US 1415183 A US1415183 A US 1415183A
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- Prior art keywords
- slag
- chamber
- furnace
- molten
- bath
- Prior art date
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Links
- 239000002893 slag Substances 0.000 description 105
- 239000000463 material Substances 0.000 description 26
- 229910052751 metal Inorganic materials 0.000 description 22
- 239000002184 metal Substances 0.000 description 22
- 239000007789 gas Substances 0.000 description 12
- 238000010438 heat treatment Methods 0.000 description 12
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 11
- 238000002485 combustion reaction Methods 0.000 description 10
- 230000001681 protective effect Effects 0.000 description 8
- 239000007788 liquid Substances 0.000 description 7
- 239000011343 solid material Substances 0.000 description 7
- 239000007787 solid Substances 0.000 description 6
- 238000003723 Smelting Methods 0.000 description 5
- 239000012530 fluid Substances 0.000 description 5
- 229910052742 iron Inorganic materials 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 239000012768 molten material Substances 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 230000001105 regulatory effect Effects 0.000 description 5
- 238000001816 cooling Methods 0.000 description 4
- 239000000446 fuel Substances 0.000 description 4
- 230000007246 mechanism Effects 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 238000007670 refining Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 239000005864 Sulphur Substances 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 239000012629 purifying agent Substances 0.000 description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- VVCMGAUPZIKYTH-VGHSCWAPSA-N 2-acetyloxybenzoic acid;[(2s,3r)-4-(dimethylamino)-3-methyl-1,2-diphenylbutan-2-yl] propanoate;1,3,7-trimethylpurine-2,6-dione Chemical compound CC(=O)OC1=CC=CC=C1C(O)=O.CN1C(=O)N(C)C(=O)C2=C1N=CN2C.C([C@](OC(=O)CC)([C@H](C)CN(C)C)C=1C=CC=CC=1)C1=CC=CC=C1 VVCMGAUPZIKYTH-VGHSCWAPSA-N 0.000 description 1
- HLLSOEKIMZEGFV-UHFFFAOYSA-N 4-(dibutylsulfamoyl)benzoic acid Chemical compound CCCCN(CCCC)S(=O)(=O)C1=CC=C(C(O)=O)C=C1 HLLSOEKIMZEGFV-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 206010073148 Multiple endocrine neoplasia type 2A Diseases 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000005255 carburizing Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000002529 flux (metallurgy) Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000003779 heat-resistant material Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000011872 intimate mixture Substances 0.000 description 1
- 239000011344 liquid material Substances 0.000 description 1
- 229910001338 liquidmetal Inorganic materials 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000010445 mica Substances 0.000 description 1
- 229910052618 mica group Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000001012 protector Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B7/00—Rotary-drum furnaces, i.e. horizontal or slightly inclined
- F27B7/02—Rotary-drum furnaces, i.e. horizontal or slightly inclined of multiple-chamber or multiple-drum type
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/56—Manufacture of steel by other methods
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B17/00—Furnaces of a kind not covered by any of groups F27B1/00 - F27B15/00
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B3/00—Hearth-type furnaces, e.g. of reverberatory type; Electric arc furnaces ; Tank furnaces
- F27B3/06—Hearth-type furnaces, e.g. of reverberatory type; Electric arc furnaces ; Tank furnaces with movable working chambers or hearths, e.g. tiltable, oscillating or describing a composed movement
Definitions
- . rlhe object of the present invention is to provide an improved apparatus for smelting and refining metalliferous material and simultaneously refining the slag produced for repeated use.
- 1 indicates a ,slag furnace, and 2 a smelting furnace
- each being lined with refractory slag-resistant material 3, between which and the wall of the furnace is preferably interposed asbestos or other heat-resistant material 3.
- Said furnaces are formed on the outside each with a series of rings or wheels 4, whichare supported by rollers 5 on shafts 6, 7, respectively, rotated by gear wheels 8, 9, respectively, meshing with gear wheels 11, 12, on shafts 13, 14, respectively, rotated from any suitable source of power.
- Saidshafts 6, 7, carry gear wheels 10,15, which mesh with gear rings 10', 15', around the furnaces 1, 2, respectively and thus positivel)v rotate said furnaces about their ⁇ axes.
- Said s hafts 8, 9, rotate in bearings 16', 17, which are supported by platforms 18, 19, which can move transversely on rollers 21, 22, so that, when desiredsaid furnaces can be moved in a direction transverse to their h.
- the slag furnace 1 and the smelting furnace 2 are supplied with fluid, o1" pul-verized solid, fuel by burners 23, 24 which enter the furnaces at one end thereof.
- the burner 24 is upheld by a hollow strap 25 water-cooled by means of pipes 26a and 26b and ,is supplied with heated air by air pipes 25, protected from being oxidized by. a coating of Figure l' v settling chamber 27,
- the protective cover of the air pipes25 may be baked or melted or in any well known manner, or the pipes lmay 'be dipped in a molten silicate such as molten slag 0r the like.
- aid pipes 25 are formed with outlet openings 25, (Fig. 3). They are connected with a main blast pipe 26.
- connection between the furnace l and the chimney 26 is made by means of ya comparatively narrow neck 29.
- the sides of the chimney next to that rthrough which the neck of the furnace enters are each cut away suiliciently to permit the neck to pass transversely through said sides, so that the neck of one slag furnace passes through one of said cutaway sides, while that of the other slag furnace passes through the opposite cutaway side.
- These cutaway sides are closed, when the furnacev is in the proper posit-ion, by chimney sections 31.
- iron ore When iron ore is to be smelted it is pulverized or comminuted, and is mixed with a' proper amount of pulverized carbon and a small quantity of suitable fiux and preferablyground with a solution of carbonate of an alkali metal, and the mixture is formed into briquettes -of a preferably spherical form so as to facilitate the feeding of the.
- Va suitable vessel in the presence of said alkaline solution an intimate mixture of said materials is obtained, thus promoting a rapid reduction of the same in the furnace.
- These briquettes are conveyed by an elevator 32 to a hopper 33 and transferred from 'said hopper, by means of a reciprocating piston 34, to an upper chute 35, continuous with a lower chute 36, communicatingy at its upper end with the hopper 33.
- the piston 34 and wheel 34 for operating the same are detachable from their support 34a when material in the form of bars ⁇ form the charge to be fed into the furnace, and the piston 34 and wheel 34 are then detached, since said bars are more conveniently 'ted into the opening filled by the piston.
- the tops of the chutes 35, 36 are trough-shaped, as shown at 36.
- the chute 36 including the trough-shaped upper side 36', is kept cooled by water conduits 50 therein.
- the chute 36 may be omitted and the chute 35 may be extended into contact with the liquid in the furnace 21.
- Into the hopper 37 is fed molten slag from the rotating furnace '1, said slag overflowing from said furnace into a conduit 20 controlled by a gate 21 and being supplied to said furnace 1 by means of a hopper 38.
- the charge and slag in the hopper 37 are heated by aVV burner 40.
- the slag is charged into the hopper 38 through the top which is afterwards closed by a shutter 41.
- Said slag is maintained hot in said hopper by means'of a burner 42, and a gate 43 shown in dotted lines, since it is on the rear side of the partition between the two compartments of the hopper 38, limits the rate at which the slag is permitted to escape by a chute 44 from the hopper.
- a chute 45 is located beneath the hopper 38 and chute 44 and discharges into the furnace.
- I provide, however, in the slag furnace 1 a bottom layer of molten iron,the depth of molten iron being suflicient only to cover the bottom of said rotating furnace and not to escape through its neck.
- the upper layer of slag escapes through the neck, leaving the iron permanently in the vessel.
- the chute 35 ⁇ removably depends from a platform 52 supported bystandards 53 and is secured to said platform by screws 72.
- the chute 36 is attached to the chute 35 by.
- a cradle 36a and strap 36b is additionally supported Lby an adjustable support 36C.
- the chute 35 When it is desired to move the furnace 2 transversely, the chute 35 is detached from the 'platform 52 and the lower chute 36, and the adjustable support 36c is lowered, so that the chute 36 extends horizontally into the furnace 2 and can thus be removed from the hole in the end of the furnace 2 through which it formerly projected.
- the upper part 27 of the settling chamber 27, which is detachable from the lower part, is also removed, carrying with it the burners and air pipes. Said upper part 27 is supported by straps 27"i having' turn buckles 27b and depend from a carriage 27c travelling on a rail 27d. l
- the briquettes and slag are fed into the furnace 2 below the surface lof the molten material therein.
- Said material consists of carburized molten metal and a layer of slag floating thereon. These are heated by the burner 24 which heats the upper part of the furnace 2 and the bath therein, and by reason of the rotation of said furnace, the heated upper portion is continually moved below the molten bath which is thereby also heated from underneath.
- the height ofthe layer is governed bythe height of a.
- cylindrical hollow slag dam 56 which is watercooled by means of an inlet pipe 57 inclosed by any outlet pipe y58 (see drawing), said pipes extending through a groove or depression formed in the bottom of'a hole in a wall 59 of said settling chamber. which is closed by a door 61, said door having therein a mica window 62 and carrying the burner 24.
- a h anger 63 which supports weights 64, by adding to or subtracting from, by which the slag dam 56 may be raised or lowered' correspondingly.
- the slag dam As the level of the slag rises inthe furnace 2, the slag dam also rises, thus permitting metal to flow underneath the" dam into the settling chamber. Since the effective weight of the slag dam' is accurately counterbalanced by the weight of the counterweight, it results that any increase in thickness of the layer of slag will cause said slag dam to rise and permit a certain amount of slag, as well as metal, to flow beneath the slag dam.
- the metal settles to the bottom of the settling chamber, and to ensure such separation by gravity the liquids in the settling chamber are maintained hot by means of a burner 66 and by the heat of the bottom of the settling chamber.
- the metal is drawn off from time to time from the settling chamber by ⁇ a tap hole 74 and the slag lis then drawn off through a hole 73 and is elevated by suitable means and discharged into the slag hopper 38.
- the slag is purified by means of a blast of steam and air through a pipe 69.
- rlhe slag is further purified in the slag furnace 1 when needed by means'of steam and air discharged through a pipe 71.
- rlhe steam is believed to purify the slag 5 in the following manner.
- ThereV is ⁇ alvvays a small quantity of metal contained in the slag, and this metal takes up the oxygen of the steam, thereby freeing' its hydrogen, which combines with the "sulphur in the slag.
- a Water jacket i8 (see Figure 1) having a stationary Wall 50 and a. Wall moving with the furnace and making a Water-tight fit With the Wall 50.
- A. roof 8l is provided to prevent gases entering the settling chamber from the furnace 2 if the apparatus is used as a refining f urnace.
- l provide Water cooling pipes, of which 82 indicates the inlet pipe and 83 the outlet pipe, said pipes 82, 83, being connected by a series of transverse pipes 84.
- 86 indicates a"conduit for carrying off gases from the settling furnace.
- the flue for the heating gases passes underneath the settling chamber' and thereby maintains the liquid metal and slag in the settling chamber in a highly heated fluid condition, this being necessary in order to better facilitate the urifying of the slag.
- Additional burners 5 are provided in case the heat from. the gases should not besufli'cient.
- metalliferous is -intended to mean ores or metals either solid or molten.
- a charge is intended to include the various materials which enter the liquid metallic bath under a molten or liquid cover.
- the liquid cover, or layer, herewithin mentioned is not necessarily a slag at the 'commencement of the process, although its composition is similar to that Off'a purified slag, but acid and basic materials in proper proportions to form a silicate compound 65 fus1ble at the temperature of the furnace may be melted down or provided from any suitable source.
- Said liquid cover acts in practice as an absorbent-of sulphur and phosphorus andsince by its use it becomes contaminated' With said impurities contained in the charge it may, afterl the commencement of the process, be properly called a slag.
- This slag needs to be purified and chemically qualified, as by the addition of acid and basic materials, or eithe'rof them alone ⁇ in order that it may be used repeatedly in the process.
- 1918 l show the charge and slag conduits extending parallel on a horizontal plane into the furnace, and such construction may be used when molten metal forms the main part of the charge, and the conduit need not be extended into the molten bath, the slag fed upon the molten metal forming a protector therefor. Said conduits being removably attached to the platform, the change is readily made.
- Oxidizing or carburizing materials or alloys acting in their well known capacities are also introduced with and form a charge or part of a charge; said material being added lin suitable quantities to bring the metal to the nature desired.
- said metal is preferably fed -in suitable lengths into the metallic bath through the flue, the detachable feed mechanism being in such case removed.
- a main chamber means for permanentlymaintain'- v "for supplying, maintaining, and withdrawing a protective cover of molten slag on and from said bath, means .for simultaneously feeding solid material and molten slag into said chamber, and means fon applying heat from both above, and below to the contents of thechamber.
- means for supplying, maintaining and withdrawing a protective cover of purified molten slag on and. from said bath means Vfor feeding a charge intosaid'bath under u said cover, means for internally heating said chamber, a-"settling chamberl to receive the vexcess of the bath andslag, means in said chamber for forcihga purifying agent on to,
- a main chamber means for permanently maintaining a metallic bath in said chamber, means for constantly supplying, maintaining and withdrawing a protective cover of purified molten slag on and from said bath,means for feeding a charge into said bath under said cover, means for applying heat from above and below to the contents of said chamber, a settling chamber to receive the excess ofthe bath and slag, means in said settling chamber for forcing a purifying agent on to the products which overflow thereinto, means for heating the bath and slag in said settling chamber from both above and below, a removable cover to prevent exhaust gases from the main chamber coming in contact with the metal in the settling chamber, means for cooling said cover,
- said settling chamber having a removable.
- a main chamber means for maintaining'- a metallic lbath in said chamber, means for feeding a chargeinto said bath, means for constantly movinggsupplying, maintaining, and withdrawing av protective cover of molten slag on and from said bath,l means forfheating"y the contents of said chamber from above Y and below, and means for emptying the A chamber.
- a main chamber means for maintaining-a metallic v bath in saidchamber, means for feeding a chargev into said bath', means for constantly drawing a protective cover of molten slag the contents of the chamber from above and moving, supplying', maintaining, and withbelow, means whereby-the thickness of said slag cover -is automatically regulated, consisting of a counter-weighted slag dam, means for cooling said dam, and means for 7.
- a main chamber means to rotate said chamber, means for maintaining a metallidbathtin said chamber, means for internally heating said chamber, separate conduits for feeding solid and molten material into said bath under a cover of slag, means for supplying,
- means for regulating the flow of said material means for cooling said conduits, and means for emptying said chamber.
- a main chamber means to rotate said chamber, means for maintaining-a metallic bath in said chamber, means for supplying, maintaining. and withdrawing a cover of molten purified slag on and from said bath, means chamber, means forinternally heating said means for rotating said chamber, means for forcing a purifying agent on to the slag in said chamber, means forl causing the fuel and products of combustion to enter and exhaust through the same end of said chamber, means for feeding solid and molten material into said chamber and means for regulating the How lof said material.
- a main chamber, and a slag chamber so placed that molten material may ow by gravity from said slag chamber into the. main chamber, means .for maintaining a metallic bath in said chambers, means for rotating the same, means for internally heating said chambers, means for causing the gases generated in said chambers to completely circulate within the same, means for feeding solid and molten material into said chambers, means for guiding the molten slag from said slag chamber into said main chamber, means for conducting away products of combustion, comprising a flue through one side of which said slag furnace enters, means in said Hue wherethrough the interiorvof the slag chamber may be seen, and means for emptying said chambers.
- a main chamber and a slag chamber means for maintaining metallic baths in ⁇ said chambers, means for internally heating the same, chambers, means for supplying, maintainingand withdrawing .
- a main chamber means for permanently maintaining ametallic bath in said chamber, means for supplying, maintaining, and withdrawing a protective cover of purified molten slag on and from said bath, means for feeding solid and liquid material into said bath,
- a main chamber a stationary platform over said chamber, a movable slag chamber supported bylsaid platform, means supported by said platform for conducting solid and molten material-into said chambers, means for preventin lthe escape of gases through the feed end o said chambers, means supported by said platform for receiving solid materials comprising an elevator and a hopper, means in the bottom of said hopper to permit said material to escape, comprising a contracted end of said hopper, opening into said conducting means, means immediately back of said opening for forcing said material into said mam chamber, .means for maintaining metallic baths in said chambers, means for supplylng, maintaining, and withdrawing molten slag on and from said baths, meaiis for purifying said slag in transit, means' material to said slag, means for feeding moli ten slag into said slag chamber, comprising a slag reservoir, means for maintaining said slag in a hot molten condition in said reservoir, means for
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
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- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture Of Iron (AREA)
Description
1. LUND.
Patented W99 R922.
Z SHEETS-fSHEET l.
METALLURGICAL APPARATUS.
APPLICATION FILED AUG.8. 1918. llgl I. I UND.
` METALLURGICAL APPARATUS. APPLICATION FILED AUG.`8, 1918.
2 SHEETS-SHEET 2.
ATrIY JOEL LUND, OF SAN FRNCISCG, CALIFORNIA.
MnmALLUnc-ICAL APPARATUS.
Lerares.
Specication ofvLetters Patent.
Patented May 9, 1922. I
Application filed August 8, 1918. Serial No. 248,854. il
To all Iwhom t may concern Be it. known that I, JOEL LUND, a citizen of the United States, residing at San Francisco, in the county of San Francisco and State of California` have invented new and useful Improvements in Metallurgical Apparatus, of which the following is a specification.
. rlhe object of the present invention is to provide an improved apparatus for smelting and refining metalliferous material and simultaneously refining the slag produced for repeated use.
n the accompanying drawings, is a longitudinal vertical section of my improved apparatus; Figures 2, 3, are translengt verse sections thereof on the lines 2 2 and 3-3 of Figure 1; Figure 4 is a broken sectional view showing a detail of Figure 3; Figure 5 is a horizontal sectional view on the line 5*,3 of Figure 1 Figure 6 is a broken side view of an upper portion of the apparatus; Figure 7 is a sectional view on the line 7-7 of Figure 1.
Referring tothe drawing, 1 indicates a ,slag furnace, and 2 a smelting furnace, the
interior of each being lined with refractory slag-resistant material 3, between which and the wall of the furnace is preferably interposed asbestos or other heat-resistant material 3. Said furnaces are formed on the outside each with a series of rings or wheels 4, whichare supported by rollers 5 on shafts 6, 7, respectively, rotated by gear wheels 8, 9, respectively, meshing with gear wheels 11, 12, on shafts 13, 14, respectively, rotated from any suitable source of power. Saidshafts 6, 7, carry gear wheels 10,15, which mesh with gear rings 10', 15', around the furnaces 1, 2, respectively and thus positivel)v rotate said furnaces about their` axes. Said s hafts 8, 9, rotate in bearings 16', 17, which are supported by platforms 18, 19, which can move transversely on rollers 21, 22, so that, when desiredsaid furnaces can be moved in a direction transverse to their h. The slag furnace 1 and the smelting furnace 2 are supplied with fluid, o1" pul-verized solid, fuel by burners 23, 24 which enter the furnaces at one end thereof. The burner 24 is upheld by a hollow strap 25 water-cooled by means of pipes 26a and 26b and ,is supplied with heated air by air pipes 25, protected from being oxidized by. a coating of Figure l' v settling chamber 27,
a silicate, or other insulating non-oxidizable material that has been melted thereon,` such coating, however, being sufficiently thin to permit the air in said pipes :to be heated by the heated gases escaping from the furnace to a flue 28. The protective cover of the air pipes25 may be baked or melted or in any well known manner, or the pipes lmay 'be dipped in a molten silicate such as molten slag 0r the like.
The connection between the furnace l and the chimney 26 is made by means of ya comparatively narrow neck 29. To permit the slag furnace-to be moved transversely after certain periods, to'bev substituted by another slag furnace, the sides of the chimney next to that rthrough which the neck of the furnace enters are each cut away suiliciently to permit the neck to pass transversely through said sides, so that the neck of one slag furnace passes through one of said cutaway sides, while that of the other slag furnace passes through the opposite cutaway side. These cutaway sides are closed, when the furnacev is in the proper posit-ion, by chimney sections 31.
When iron ore is to be smelted it is pulverized or comminuted, and is mixed with a' proper amount of pulverized carbon and a small quantity of suitable fiux and preferablyground with a solution of carbonate of an alkali metal, and the mixture is formed into briquettes -of a preferably spherical form so as to facilitate the feeding of the.
Va suitable vessel in the presence of said alkaline solution, an intimate mixture of said materials is obtained, thus promoting a rapid reduction of the same in the furnace. These briquettes are conveyed by an elevator 32 to a hopper 33 and transferred from 'said hopper, by means of a reciprocating piston 34, to an upper chute 35, continuous with a lower chute 36, communicatingy at its upper end with the hopper 33. The piston 34 and wheel 34 for operating the same are detachable from their support 34a when material in the form of bars `form the charge to be fed into the furnace, and the piston 34 and wheel 34 are then detached, since said bars are more conveniently 'ted into the opening filled by the piston. The tops of the chutes 35, 36, are trough-shaped, as shown at 36. The chute 36, including the trough-shaped upper side 36', is kept cooled by water conduits 50 therein. The chute 36 may be omitted and the chute 35 may be extended into contact with the liquid in the furnace 21. Into the hopper 37 is fed molten slag from the rotating furnace '1, said slag overflowing from said furnace into a conduit 20 controlled by a gate 21 and being supplied to said furnace 1 by means of a hopper 38.
' The charge and slag in the hopper 37 are heated by aVV burner 40. The slag is charged into the hopper 38 through the top which is afterwards closed by a shutter 41. Said slag is maintained hot in said hopper by means'of a burner 42, and a gate 43 shown in dotted lines, since it is on the rear side of the partition between the two compartments of the hopper 38, limits the rate at which the slag is permitted to escape by a chute 44 from the hopper. A chute 45 is located beneath the hopper 38 and chute 44 and discharges into the furnace. Basic or acid material as may be found necessary to properly proportion the slag to render it more fluid and a more eliicient fluxing agent is contained in the said chute 45 and hopper 37 and is conveyed as desired by means of a feed screw -47. The chute 44 discharges into the end of the rotating furnace 1 opposite to the burner 23, and the chutes 44 and 45 are maintained comparatively cool by means ofa water jacket 48 therearound. Said hoppers are supported upon a suitable frame 49, which can be moved to and from the furnace 1 by means of rollers 51.
I provide, however, in the slag furnace 1 a bottom layer of molten iron,the depth of molten iron being suflicient only to cover the bottom of said rotating furnace and not to escape through its neck. The upper layer of slag escapes through the neck, leaving the iron permanently in the vessel.
The chute 35` removably depends from a platform 52 supported bystandards 53 and is secured to said platform by screws 72.
The chute 36 is attached to the chute 35 by.
a cradle 36a and strap 36b and is additionally supported Lby an adjustable support 36C.
When it is desired to move the furnace 2 transversely, the chute 35 is detached from the 'platform 52 and the lower chute 36, and the adjustable support 36c is lowered, so that the chute 36 extends horizontally into the furnace 2 and can thus be removed from the hole in the end of the furnace 2 through which it formerly projected. The upper part 27 of the settling chamber 27, which is detachable from the lower part, is also removed, carrying with it the burners and air pipes. Said upper part 27 is supported by straps 27"i having' turn buckles 27b and depend from a carriage 27c travelling on a rail 27d. l
By the chute 36 and trough 36 the briquettes and slag are fed into the furnace 2 below the surface lof the molten material therein. Said material consists of carburized molten metal and a layer of slag floating thereon. These are heated by the burner 24 which heats the upper part of the furnace 2 and the bath therein, and by reason of the rotation of said furnace, the heated upper portion is continually moved below the molten bath which is thereby also heated from underneath. The height ofthe layer is governed bythe height of a. cylindrical hollow slag dam 56 which is watercooled by means of an inlet pipe 57 inclosed by any outlet pipe y58 (see drawing), said pipes extending through a groove or depression formed in the bottom of'a hole in a wall 59 of said settling chamber. which is closed by a door 61, said door having therein a mica window 62 and carrying the burner 24. Upon the outer end of the pipe 58 'is a h anger 63 which supports weights 64, by adding to or subtracting from, by which the slag dam 56 may be raised or lowered' correspondingly.
As the level of the slag rises inthe furnace 2, the slag dam also rises, thus permitting metal to flow underneath the" dam into the settling chamber. Since the effective weight of the slag dam' is accurately counterbalanced by the weight of the counterweight, it results that any increase in thickness of the layer of slag will cause said slag dam to rise and permit a certain amount of slag, as well as metal, to flow beneath the slag dam. The metal settles to the bottom of the settling chamber, and to ensure such separation by gravity the liquids in the settling chamber are maintained hot by means of a burner 66 and by the heat of the bottom of the settling chamber. The metal is drawn off from time to time from the settling chamber by `a tap hole 74 and the slag lis then drawn off through a hole 73 and is elevated by suitable means and discharged into the slag hopper 38.
Before so drawing it olf from the settling chamber the slag is purified by means of a blast of steam and air through a pipe 69.
rlhe slag is further purified in the slag furnace 1 when needed by means'of steam and air discharged through a pipe 71.
rlhe steam is believed to purify the slag 5 in the following manner. ThereV is `alvvays a small quantity of metal contained in the slag, and this metal takes up the oxygen of the steam, thereby freeing' its hydrogen, which combines with the "sulphur in the slag.
At all junctures of open ends of the furnaces 1 and 2 with stationary parts, as the chimney 26, -4the chutes 44, 45, and 35, and the settling chamber 27, there is provided a Water jacket i8 (see Figure 1) having a stationary Wall 50 and a. Wall moving with the furnace and making a Water-tight fit With the Wall 50.
A. roof 8l is provided to prevent gases entering the settling chamber from the furnace 2 if the apparatus is used as a refining f urnace. To maintain the vroof 81 comparatively cool, l provide Water cooling pipes, of which 82 indicates the inlet pipe and 83 the outlet pipe, said pipes 82, 83, being connected bya series of transverse pipes 84. 86 indicates a"conduit for carrying off gases from the settling furnace. When molten iron forms part of the charge, fthe door 87 in the chimney 26 is opened and the fluid iron from a blast furnace or mixer is poured through said opening by a suitable conduit, and it mixes with the slag inthe flue 'in which said slag is carried down into the chamber and is decarlourized by the oxygen of the ore or other oxidizing agents fed in suitable quantities into the furnace chamber by means of conduit 36.
In case solid metal is the main portion of the charge l preferably introduce it into the furnace by removing thedetachable .feed mechanism and feeding it through the chute rin which said mechanism operates and I also feed proper portions of slag and qualifying agents. l
As shown at.28 in Figure 3, the flue for the heating gases passes underneath the settling chamber' and thereby maintains the liquid metal and slag in the settling chamber in a highly heated fluid condition, this being necessary in order to better facilitate the urifying of the slag. Additional burners 5 are provided in case the heat from. the gases should not besufli'cient.
The term metalliferous is -intended to mean ores or metals either solid or molten.
The term a charge is intended to include the various materials which enter the liquid metallic bath under a molten or liquid cover. The liquid cover, or layer, herewithin mentioned, is not necessarily a slag at the 'commencement of the process, although its composition is similar to that Off'a purified slag, but acid and basic materials in proper proportions to form a silicate compound 65 fus1ble at the temperature of the furnace may be melted down or provided from any suitable source.
Said liquid cover acts in practice as an absorbent-of sulphur and phosphorus andsince by its use it becomes contaminated' With said impurities contained in the charge it may, afterl the commencement of the process, be properly called a slag. This slag, however, needs to be purified and chemically qualified, as by the addition of acid and basic materials, or eithe'rof them alone` in order that it may be used repeatedly in the process.
Fluxes or mixtures already known to be used in smelting and refining to bring about certain results are introduced with, and form a part of, a charge and retain their advantages in my process, with this additional advantage, that the molten slag or liquid cover which continuously enter the furnace in a purified and chemically qualified condition also acts as an effective flux. In m application Serial No. 211,269, filed Jan. 10,
1918 l show the charge and slag conduits extending parallel on a horizontal plane into the furnace, and such construction may be used when molten metal forms the main part of the charge, and the conduit need not be extended into the molten bath, the slag fed upon the molten metal forming a protector therefor. Said conduits being removably attached to the platform, the change is readily made. When itis desirable to treat with only a limited amount of material at a time or that the metallic bathiitself should be treated to form a finished product, my process is equally applicable in that I supply, maintain, and Withdraw, to, on, and from the said bath, the repeatedly purified and qualified slag, which forms a protective cover thereon, and when there is not a suflicient quantity of the metallic bath inthe furnace to cause the slag to overflow into the settling chamber, then the excess of slag covering. said bath maybe Withdrawn by means of a hand rake through the door and opening, the slag dam being in 4such case removed, .and the finished metal being withdrawn through tap hole 75.
It being Well known in metallurgy that Wet material submerged in a metallic bath Will cause explosion, it is understood that all materials composing a charge, yand which 'are to be submerged in said, bath', must previously have had the moisture expelled by any well-known means vvh'ether this be spe- `cifically stated or not.
When it is `desirable to produce an unusu ally basic slag in furnace 1, to take up the sulphur and phosphorus from the metalliferous material in furnace 2, this is accomv plished by adding lbasic material lto the molten purified slag in furnace 1 by means of the hopper and feed mechanism, as shown, said basic material'being melted down While 130 mixing with the molten slag in furnace l.
'As such a composition requires high heat to melt and remain fluid it is desirable that. most of the steaming of the slag be done in the settling chamber 27, as thereby the heat produced by combustion of fuel in the chamber 1 is utilized for smelting said basic material. l
Oxidizing or carburizing materials or alloys acting in their well known capacities are also introduced with and form a charge or part of a charge; said material being added lin suitable quantities to bring the metal to the nature desired.
When solid metal is the main part of a charge, said metal is preferably fed -in suitable lengths into the metallic bath through the flue, the detachable feed mechanism being in such case removed.
Other solid ingredients which form the balance of said charge are fed simultaneously into said bath from the hopper through the conduit.
Thenature of the charge and the uses to which the metal produced is to be put being known, by examining from time to time the molten metal overflowing into the settling chamber, the speed of feeding andthe length of treatment necessary may be determined and also'whether any well known modifications of the components of such charge are needed to facilitate the operation and attain ing a metallic bath in said chamber, means.'l
the best results. When molten metal direct from the blast furnace or mixer constitutes the main ortion of the charge, said metal is introduce through a door in the chimney 26 and is fed together with the purified sla@r into the metallicbath in furnace 2 by mean@ ofthe slag spout.v f
I claim:-
1. In a metallurgical apparatus, a main chamber, means for permanentlymaintain'- v "for supplying, maintaining, and withdrawing a protective cover of molten slag on and from said bath, means .for simultaneously feeding solid material and molten slag into said chamber, and means fon applying heat from both above, and below to the contents of thechamber.
2. In' a metallurgical apparatus, a ,main chamber, a metallic bath in said chamber,
means for supplying, maintaining and withdrawing a protective cover of purified molten slag on and. from said bath, means Vfor feeding a charge intosaid'bath under u said cover, means for internally heating said chamber, a-"settling chamberl to receive the vexcess of the bath andslag, means in said chamber for forcihga purifying agent on to,
' the products which overflow'thereinto, means i for heatingthe bath and slag in said settling chamberfrom both above and below, means for preventingexhaust gases from the main chamber `entering the settling chamber,
emptying the chamber.
means whereby the gas generated in said settling chamber may escape, and lmeans for the I separate withdrawal of slag and metal from said settling chamber.
3. In a metallurgical apparatus, a main chamber, means for permanently maintaining a metallic bath in said chamber, means for constantly supplying, maintaining and withdrawing a protective cover of purified molten slag on and from said bath,means for feeding a charge into said bath under said cover, means for applying heat from above and below to the contents of said chamber, a settling chamber to receive the excess ofthe bath and slag, means in said settling chamber for forcing a purifying agent on to the products which overflow thereinto, means for heating the bath and slag in said settling chamber from both above and below, a removable cover to prevent exhaust gases from the main chamber coming in contact with the metal in the settling chamber, means for cooling said cover,
said settling chamber having a removable.
upper portion, means for supporting and guiding said portion while it' is being moved, and means removably attached' to Vsaid upper portion whereby exhaust gases that molten slag can flow by gravity fromsaid reservoir through said slag chamber `and main chamber into said settling cham` ber, means -for maintaining said slag -in a hot molten condition in said reservoir, and means for heating said slag in transit.
5. In a' metallurgical apparatus, a main chamber, means for maintaining'- a metallic lbath in said chamber, means for feeding a chargeinto said bath, means for constantly movinggsupplying, maintaining, and withdrawing av protective cover of molten slag on and from said bath,l means forfheating"y the contents of said chamber from above Y and below, and means for emptying the A chamber.
- 1 6. In a metallurgical apparatus, a main chamber, means for maintaining-a metallic v bath in saidchamber, means for feeding a chargev into said bath', means for constantly drawing a protective cover of molten slag the contents of the chamber from above and moving, supplying', maintaining, and withbelow, means whereby-the thickness of said slag cover -is automatically regulated, consisting of a counter-weighted slag dam, means for cooling said dam, and means for 7. In ametallurgical apparatus, a main chamber, means to rotate said chamber, means for maintaining a metallidbathtin said chamber, means for internally heating said chamber, separate conduits for feeding solid and molten material into said bath under a cover of slag, means for supplying,
,maintaining and withdrawing said cover,
means for regulating the flow of said material, means for cooling said conduits, and means for emptying said chamber.
8. In a metallurgical apparatus, a main chamber, means to rotate said chamber, means for maintaining-a metallic bath in said chamber, means for supplying, maintaining. and withdrawing a cover of molten purified slag on and from said bath, means chamber, means forinternally heating said means for rotating said chamber, means for forcing a purifying agent on to the slag in said chamber, means forl causing the fuel and products of combustion to enter and exhaust through the same end of said chamber, means for feeding solid and molten material into said chamber and means for regulating the How lof said material.
9. In atmetallurgicaldapparatus, a main chamber, and a slag chamber so placed that molten material may ow by gravity from said slag chamber into the. main chamber, means .for maintaining a metallic bath in said chambers, means for rotating the same, means for internally heating said chambers, means for causing the gases generated in said chambers to completely circulate within the same, means for feeding solid and molten material into said chambers, means for guiding the molten slag from said slag chamber into said main chamber, means for conducting away products of combustion, comprising a flue through one side of which said slag furnace enters, means in said Hue wherethrough the interiorvof the slag chamber may be seen, and means for emptying said chambers. i
10. In a metallurgical apparatus, a main chamber and a slag chamber, means for maintaining metallic baths in` said chambers, means for internally heating the same, chambers, means for supplying, maintainingand withdrawing .a
coverof molten slag on and from the baths 1n said chambers, means for purifying said 1t flows through the slag chamber, ineans for guiding thefmolten slag as it flows from said slag chamber into the main chamber, means for heating the slag' in transit, means for feeding molten slag and solid material into said slag chamber comprising a movable reservoir divided into compartments, conduits from said compartments, wherethrough the molten slag and granulated material may be fed, the former immediately above the latter, into said slag chamber, and means for regulating the flow of said slag and material.
11. In a metallurgical apparatus, -a main chamber,v means for permanently maintaining a metallic bath in said chamber, a burner in said main chamber for heating said bath,
means for' blowing into said chamber air for combustion of the fuel from said burner, means for circulating the products of combustion entirely around the interior of the said main chamber, means for heating said air for combustion, comprising a removable portion of, and over, a settling chamber,
means in said removable portion forconducting said air for combustion through the same into said main chamber, and means for causing said products of combustion to pass in close proximity to said air conducting means in said removable portion of said settlingl chamber.
12. In a metallurgical apparatus, a main chamber, means for permanently maintaining ametallic bath in said chamber, means for supplying, maintaining, and withdrawing a protective cover of purified molten slag on and from said bath, means for feeding solid and liquid material into said bath,
comprising supports adjacent'to said main chamber, a conduit removably attached to said supports,aand a piston reciprocating in the. conduit and removably attached to others of said supports adjacent thereto, means for regulating the ow of material intosaid main chamber, and means for applying heat from above and below to the cony tents of the chamber.
13. In a metallurgical apparatus, a main chamber, a stationary platform over said chamber, a movable slag chamber supported bylsaid platform, means supported by said platform for conducting solid and molten material-into said chambers, means for preventin lthe escape of gases through the feed end o said chambers, means supported by said platform for receiving solid materials comprising an elevator and a hopper, means in the bottom of said hopper to permit said material to escape, comprising a contracted end of said hopper, opening into said conducting means, means immediately back of said opening for forcing said material into said mam chamber, .means for maintaining metallic baths in said chambers, means for supplylng, maintaining, and withdrawing molten slag on and from said baths, meaiis for purifying said slag in transit, means' material to said slag, means for feeding moli ten slag into said slag chamber, comprising a slag reservoir, means for maintaining said slag in a hot molten condition in said reservoir, means for feeding aA charge into'the bath in the main chamber, means for maintaining and withdrawing a cover of molten slag of predetermined thickness over the bath in said main chamber, meansfor internally heating said chamber, and means for emptying the chamber.
JOEL LUND.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US248854A US1415183A (en) | 1918-08-08 | 1918-08-08 | Metallurgical apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US248854A US1415183A (en) | 1918-08-08 | 1918-08-08 | Metallurgical apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1415183A true US1415183A (en) | 1922-05-09 |
Family
ID=22940960
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US248854A Expired - Lifetime US1415183A (en) | 1918-08-08 | 1918-08-08 | Metallurgical apparatus |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1415183A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2750286A (en) * | 1952-06-21 | 1956-06-12 | Electro Chimie Metal | Production of iron-nickel alloys from low grade ores |
| US2770021A (en) * | 1952-10-23 | 1956-11-13 | Babcock & Wilcox Co | Method of and apparatus for continuous casting |
| US2855194A (en) * | 1954-07-21 | 1958-10-07 | Brassert Oxygen Technik A G | System for sealing a converter |
| US2859106A (en) * | 1952-09-17 | 1958-11-04 | Antonsen Randolph | Process and apparatus for removing sulfur from iron |
| US3215425A (en) * | 1953-12-28 | 1965-11-02 | Kaiser Ind Corp | Metallurgical apparatus |
| US3326670A (en) * | 1965-07-16 | 1967-06-20 | Billy B Bratton | Steelmaking process |
| US3941585A (en) * | 1971-02-19 | 1976-03-02 | Edward C. Levy Company | Process for cooling slag and inhibiting pollutant formation |
-
1918
- 1918-08-08 US US248854A patent/US1415183A/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2750286A (en) * | 1952-06-21 | 1956-06-12 | Electro Chimie Metal | Production of iron-nickel alloys from low grade ores |
| US2859106A (en) * | 1952-09-17 | 1958-11-04 | Antonsen Randolph | Process and apparatus for removing sulfur from iron |
| US2770021A (en) * | 1952-10-23 | 1956-11-13 | Babcock & Wilcox Co | Method of and apparatus for continuous casting |
| US3215425A (en) * | 1953-12-28 | 1965-11-02 | Kaiser Ind Corp | Metallurgical apparatus |
| US2855194A (en) * | 1954-07-21 | 1958-10-07 | Brassert Oxygen Technik A G | System for sealing a converter |
| US3326670A (en) * | 1965-07-16 | 1967-06-20 | Billy B Bratton | Steelmaking process |
| US3941585A (en) * | 1971-02-19 | 1976-03-02 | Edward C. Levy Company | Process for cooling slag and inhibiting pollutant formation |
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