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Publication numberUS2980596 A
Publication typeGrant
Publication dateApr 18, 1961
Filing dateDec 27, 1956
Priority dateDec 27, 1956
Publication numberUS 2980596 A, US 2980596A, US-A-2980596, US2980596 A, US2980596A
InventorsConway George E
Original AssigneeConway George E
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Electrolytic reduction furnace constructions and method
US 2980596 A
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Description  (OCR text may contain errors)

April 18, 1961 Filed Deo. 27, 1956 G. E. CONWAY 2,980,596


April 18, 1961 G. E. CONWAY ELECTROLYTIC REDUCTION FURNACE CONSTRUCTIONS AND METHOD Filed Dec. 27, 1956 3 Sheets-Sheet 2 AUTOR/V56 April 18, 1961 G. E. CONWAY 2,980,596

ELECTROLYTIC REDUCTION FURNACE CONSTRUCTIONS AND METHOD Filed Dec. 27. 1956 3 Sheets-Sheet 5 I N V EN TOR. 63501265 E. Co/vA/v/ @mm v- M A fram/fw ELECTROLYTIC REDUCTION FURNACE CON- STRUCTIONS AND METHOD George E. Conway, 33 Mezzine Drive, 'CresskilL NJ. Filed Dec. 27, 1956, Ser. No. 630,914

11 Claims. (Cl. 204-67) This invention relates to electrolytic reduction furnace constructions, such as used in aluminum production and other like purposes, and the method features of operation thereof.

Among the objects of the invention is to generally iml prove electrolytic reduction furnace constructions of the character described and the method of operation thereof, which construction shall comprise few and simple parts assembled to form a compact easily operating apparatus by a method requiring a minimum of supervision, attention and maintenance, which shall provide a ready means and method of operation for keeping the furnace in most efficient operation, which shall feature a horizont-ally disposed cylindrically shaped anode mounted for axial rotation to alternately immerse opposite surfaces thereof in a molten electrolyte, which anode shall initially be provided with a prebaked surface of carbon paste and be arranged for subsequent refinishing in situ, whichv construction and method provide and maintain uniform spacing between anode and cathode, which shall be capable of giving productive service with less operational adjustment than heretofore, which construction shall be rel-atively inexpensive to manufacture and which shall be efficient and practical to a high degree in use.

Other objects of the invention will in part be obvious and in part hereinafter pointed out;

The invention accordingly consists of features of constructions and method, combinations of elements and arrangements of parts which will be exemplified in the constructions and method hereinafter disclosed, the scope of the application of which will be indicated in the claims following.

This application is a continuation-in-part of my application Serial No. 412,310, filed February 24, 1954, now abandoned, entitled Electrolytic Reduction Furnace Construction and Method of Operation.

In the accompanying drawing in which embodiments of the invention are shown:

Fig. 1 is a transverse sectional View taken on line 1-1 in Fig. 2 of an improved electrolytic reduction furnace construction embodying the invention having a cylindrical anode mounted for rotation on its horizontally disposed axis.

Fig. 2 is a shortened longitudinal vertical sectional view taken on line 2-2 in Fig. 1 showing details o-f said improved construction, a mid-portion thereofy being broken away.

Fig. 3 is a detailed fragmentary cross-sectional View taken on line 3 3 in Fig. 2 showing details of an end bearing stnucture.

Fig. 4 is an elevational end View of said improved furnace construction shown in Figs. l to 3, and

Figs. 5 and 6 are views each similar to Fig. 1 showing the general contour of various other illustrative crosssectional shaped improved anode and pot portion `furnace constructions that may be employed in practicing the invention.

Referring in detail to the drawing, denotes an Patented Apr. 18, 1961 electrolytic reduction furnace construction embodying the invention, here shown for example, `as used' for the production of aluminum.

Furnace construction 10 here shown may comprise an elongated cylindrical anode 11 positioned with an axis XX thereof horizontally disposed and fitted to have a curved peripheral surface portion 11a thereof positioned to extend down into a pot portion 12 in an operative spaced relation from a cathode lining 12a of the latter and may normally be in a substantially concentric relation with respect to said anode surface portion 11a, as is clear from Figs. 1, 2 and 4.

Anode 11 may comprise a body Aportion including a metallic current carrying tube 11b terminated at opposite ends 11j thereof by spider hubs llc from which outwardly project shafts 11d and 11d'. Shafts 11d and 11a" are aligned along said axis X-X about which said anode tube 11b may be rotated in journal heat'insulating bearing blocks 11m carried in spaced apart horizontally disposed cradle cross bars 11n. The latter have the opposite ends thereof joined for support with spaced apart longitudinally extending bafiie members 11r `and are heat insulated from anode 11 by suitably inserted liners or shims 10a, asis clear from Fig. 2. The enclosure formed by said bafiie members 11r and said cradle cross bars 11n encircling anode 11 is supported from horizontally extending parallelly aligned I-beams 11q with said cradle bars 11n dependingly mounted from said beams 11g through suitable end level adjusting means, such as, for example, hanger bolts 11p. An end of shaft 11d beyond bearing block 11m shown broken away in Fig. 2 may he made to extend beyond .furnace 10 for connection with any suitable means (not shown) for rotating anode 11 on its axis X-X in the manner and for the purpose hereinafter described.

As is clear from Figs. l, 2 and 3, since I-beams 11q together with baffies 11r, hanger bolts 11p, cradle cross barns 11n and anode 11 are mounted in position to `form an adjustable assembly for the latter, said assembly may be electrically insulated from relatively stationary chanly insulated byV block liners orshims 10d. Said assem-v bly, therefore, through hanger bolts 11p can be made effective for lowering or raising anode 11 to set the gap or distance D between the anode surface portion 11a and underlying liner cathode 12a.

Extending radially outward from said anode tube 11b in spaced apart staggered Vcircumferential rows, there are provided metallic electric current distributor studs or extensions 11e. The latter serve to conduct the current from the anode tube 11b through a bed or covering layer of heat insulating material 11f extending about outer surface of tube 11b and partly about studs 11e. -Said insulating layer 113 may be of a thickness to reach a midsection of the length of studs 11e with the remaining free end portions thereof firmly embedded in current carrying contact with a surrounding shell of carbon material 11h, a down facing portion of which provides lthe effeo tive electrical terminal below bath level L of molten electrolytic material E comprising cryolite with alumina dissolved therein. From the molten bath of said material E, aluminum prod-uct `A is extracted in pot portion 12 which flows down into reservoir 12f, as is clear from Figs. 1 and 2. l

To confine said heat insulating layer 11f as a compact body and -against accidental crumbling at opposite ends thereof wherethrough anode end terminals 11]' extend, there may be provided suitable fitted disc closures 11k. Said anode end terminals 11]' may be joined in electrical circuit with positive side of an electric power cable 13 extending from a suitable suppl-y source (not shown) in the well understood manner through suitable connectors, such as, terminal clamp rings 13a, as is clear from Figs. 2 and 4.

Pot portion 1'2 may have said cathode lining 12a thereof formed of current carrying carbon block sections or bricks fitted together inside box-like framework 12C to provide a trough 12d of arcuate cross-sectional shaped contour in which said material E is retained until the molten aluminum product A produced gravitates through passageways 12e into lined reservoir 12f in establishing an operative bath level L in trough 12d. Said passageways 12e may be channeled down through an inverted keystone or center carbon brick 12g ofl cathode lining 12a and reservoir 12f hollowed out of or otherwise formed in carbon brick structure 12h in the underportion of cathode lining 12a, as is clear `from Figs. l and 2.

Box-like framework 12e may be constructed to include a suitable casing 12p for enclosing the bottom, sides and ends of pot portion 12 braced by angle members 12g extending along the edges thereof and spaced apart beams 12k serving as bottom ties and supporting structure for the casing and contents thereof. Suitable sheet material sheathing 12j having heat insulating properties is provided between casing 12p and the cathode lining 12a.

As part of the electrical circuit associated with cathode lining 12a, there is provided metallic load and current carrying tubes 12m which may be alternately spaced apart with respectrto tie beams 12k and held in direct electric contact along the length thereof by being tightly fitted and cemented with a suitable carbon paste in channeled portions 12n provided on the down facing side of the various block sections comprising cathode lining 12a, as is clear from Fig. l.

The entire pot portion 12 may be rigidly supported from the iloor or ground G in yany suitable manner, as for example, on a centrally extending main I-beam 12r resting on end piers 12s rigidly secured by bolts 12:* anchored to iioor G. Said framework 12e as Well as the entire cathode pot portion 12 may be electrically insulated from the ground by providing insulating means itis between said end piers 12s and I-beam 121-, as is clear from Figs. l and 4. Additional spaced apart bracing means, such as, guy rods 12u also suitably insulated from ground G may be provided, each fastened Ito a block pier 12v secured by oor anchoring bolts 12w.

Metallic tubes 12m serve as distributed circuit current collectors for the electrical power passing from anode 11 through lining cathode 12a. The latter may be connected in circuit in any suitable manner as by riveted joints 12y with each tube 12m through cables or bus bars 12x to the electric power negative side which extends from said power supply source (not shown).

Anode 11 when not in operation may be positioned with sufficient clearance with respect to encircling baille members 11r and cradle bars 11n so as not to interfere with turning movement given anode 11 in bearing blocks 11m whereby inspection of anode surface portion 11a is facilitated and giving ready access for reconditioning and repairing of any section of anode surface portion 11a as required. Anode 11, when in operation, may have spaces forming said clearance caulked with a removable suitable packing of clay or other suitable material as at c to prevent leakage or seepage of combustible Waste gas confined under baflie members 111', as is clear from Fig. l.

Baiie members 11r and cradle bars 11n may be formed to provide upfacing inlet feeding openings 11s for furnace construction 10 into which the required granulated cryolite and alumina comprising said material E are dumped or shoveled in proper sequence 'during operation thereof.

Since combustible waste gases are continuously given off from the molten material in furnace construction 10 being subjected to the electrolytic reduction, there may be provided one or more suitable burners 14 which may 4 be mounted by pipe fittings 14a to connect with the underside of baflie members 11r so that combustible gases generated during the operation collect and rise up, pass through iittings 14a and are consumed by burners 14 thereby safely disposing of such gases.

Suitable carbon material may be utilized for forming carboniferous shell 11h of the anode as well as the various blocks forming the lining of cathode 12a. In the iirst instance, shell 11h and cathode 12a may be made of similar composition, as for example, from pulverized coal and coke bound with pitch or asphalt into a paste which is formed into required shapes in a mold and then cured to hardness by baking in an oven at suitable temperatures. The composition of these carbon pastes and method of forming into cathode structure are well known in the art.

After assembling furnace construction 10 from the parts and in the manner shown and described, the anode 11 by means of level adjusting hanger bolts 11p is adjusted to bring anode carbon surface portion 11a and the surface of cathode lining 12a in contact. Granulated cryolite is then poured through said inlet feeding openings 11s into pot portion 12 between the surfaces of the cathode lining 12a and anode surface portion 11a not in contact. On energizing the circuit, the current passing from power cables 13 through ring connectors 13a to anode tube 11b and from studs 11e is distributed through anode surface portion 11a for the heating operation that will cause the cryolite to melt. The anode surface portion 11a from said contacting position is then lifted and gradually adjusted by hanger bolts 11p until a gap distance D in a proper operating desired range is reached while more cryolite is added and melted until a bath thereof is provided in the furnace construction 10 between said anode surface portion 11a and cathode trough 12d.

A charge of alumina E is next fed into openings 11s which dissolves in the molten cryolite. The heated alumina E froths up into said openings 11s and forms a crust E' sealing the latter over bath level L. As the furnace 10 continues in operation, the alumina E dissolved in the bath is reduced by electrolysis to aluminum metal A which collects at the cathode and being in a molten state at the operating temperatures of the furnace gravitates downpassageways 12e into reservoir 12j. Thus, current from the anode surface portion 11a is passed through the electrolytic bath to the cathode liner 12a and is collected by the distributed cathode tubes 12m to ow through bus bars 12x and generally m-ay then be passed to one or more other furnaces 10 connected in series.

It should be noted that anode 11 has hollow current carrying anode tube 11b incorporated with layer 11f of -a suitable refractory material such as, asbestos wool, fire brick, or similar material, as a heat insulated structure and by means of the openings in spider hubs 11C is provided with circulation of cooling air through its hollow center. Anode 11 also has the arrangement of the free ends of the staggered radially extending current distributing studs 11e permanently embedded in carbon shell 11h for effective and even distribution of power so that anode 11 may be intermittently turned in bearing blocks 11m when found necessary for maintaining a smooth relatively unpitted section of surface portion 11a immersed in the molten material being subjected to electrolytic reduction :action so as to practically eliminate the trapping of gases along said anode surface portion 11a thereby increasing the operation eiiiciency.

As described above, anode surface portion 11a is of curved construction, gases evolved and rising during the electrolytic reduction operation are not trapped or do not readily adhere thereon but are more readily guided to float free from the molten electrolyte bath which is desirable. Since less th-an onehalf of said surface portion 11a is used during each continuous run of operation of furnace accorse construction 10, such surface portion 11a in use that may require inspection, maintenance or rebuilding can be readily attended to by simply turning anode 11 in cradle bearing blocks 11m on axis X-X by suitable hand or power means connected to axial shaft l11d to bring said consumed surface portion 11a in a fully exposed upfacing position for working thereon while furnace construction continues to operate with another anode surface portion 11a positioned in effective immersed position.

A further improved feature is provided bythe arrangement of said cathode tubes 12my which may be aircooled internally and externally and by the provision of reservoir 12j positioned at a level to receive the molten metal A by gravity for draining the latter down from gap D and reducing to a minimum the necessity or readjusting the gap distance D for best electrolytic reduction action.

As the electrolytic reduction action in furnace construction 10 continues, outlet valve 15 provided for reservoir 12]c is tapped to withdraw the molten aluminum product A from time to time keeping the trough space at gap D drained.

One of the primary objects of this invention is to provide a novel furnace construction and method of operation whereby the distance D between the anode and cathode surfaces is maintained substantially uniform at all times and whereby the consumed surface of the anode is reinished periodically without interruption of operation. To this end, electric current distributing studs 11e are permanently embedded in anode 11 and extend radially to terminate a sufficient distance short of anode surface 11a to prevent exposure thereof due to consumption of carbon shell 11h at .said surface 11a during intended normal operation of furnace 10. This distance or thickness of shell beyond said stud ends may vary from about three to nine inches depending on the overall diameter of the anode.

Furnace construction 10 may be built in a Wide range of sizes, for example, to accommodate anodes 11 from three to twelve feet in diameter and in lengths from one to two times the diameter..

In operation, furnace 10 may be expected to consume that portion of carbon shell 11h immersed in the electrolyte E up to a depth of 3A of an inch during a twentyfour hour period of operation. Thus, by changing the immersed surface portion every eight hours, replenishment and refinishing of the consumed surface will be required only to an average depth of 1A of an inch. This is readily accomplished by utilizing a carbon paste similar in composition to that used in originally forming carbon shell 11h as hereinbefore described. This layer of new carbon paste is applied by any suitable means at a temperature of about 150 C. (known as the spreading point) which imparts a plastic workable spreading consistency to the paste.

The upturned surface portion of anode 11 during normal operation of furnace 10 will be kept at a temperature of about 200 C. to 300 C. by the radiation of heat from the electrolytic bath E which operates at about 900 C. toV 950 C.

Thus, it will be observed that by applying the refinishing carbon paste at the beginning ofthe period following rotation of anode 11, the newly formed surface will have ample time for said heat radiation to drive off most of the Ivolatile components of the paste material so that the renished portion will be partly cured to a semihardened state. At the end of said period, anode 11 is rotated, exposing a newly consumed portion of surface y 11a and introducing said reinished and partly cured portion into the molten electrolytic bath E. Said 1A inch thick semi-hardened partly cured renished portion on contact with the molten material E will quickly fry and form into a hardened crust that becomes electrically conductive for continuing the proper functioning of anode 11. Said frying may be accompanied by sizzling of the newly applied and partly cured layer of carbon paste along the line of entry, anode 11 being rotated at a rate of about one linear foot of circumference per second to effect the change-over to a refinishing surface in operative position immersed in said molten material E in a relatively short period of time. The clamp ring connectors 13a at bolt and nut 13b may be loosened sufficiently to permit rotation of anode 11 but otherwise it is intended that the current be permitted to continue owing through furnace 11 while said rotation'is being accomplished.

It is to be understood that the consumed surface portion of the opposite ends 11t of anode shell 11h will likewise be relinished as required.

From the above, it is seen that the resulting improved method may include the steps of electrically energizing the furnace construction 10 for continuous reduction operation of molten material E while intermittently drawing off excess molten reduced product A and keeping the anode 11 and cathode pot portion 12 in a desired adjusted substantially constant spaced relation. Under normal operating conditions, a gap distance D of about two inches will give satisfactory results,4 although this may be varied when found desirable. Said continuous operation is maintained by adding alumina periodically as needed, this being accomplished in-the well understood manner by breaking away portions of crust E' which seals the openings 11s. i i As described hereinbefore, when anode 11 requires refinishing after a predetermined time interval of operation, the seal formed by caulking at 10c is broken away and anode 11a rotated on axis X--X to move a first portion of anode surface 11a which has been consumed to a desired degree out of effective registering alignment lwith cathode pot portion lining 12a while simultaneously ties. Rotation of anode 11 is continued until an entirely new surface is brought into -proper register with said cathode surface 12a and said irst consumed portion is accessible for rebuilding and refinishing. Caulking at 10c is then restored and said iirst consumed portion of anode surface 11a reiinished as hereinbefore described. By carrying on this method in successive cycles, furnace 10 is kept in continuous operation for long periods of time without delays or shutdowns and at a minimum of maintenance costs.

While the above description suggests utilizing eight hour intervals between successive rotations of the anode, this is to be taken as illustrative since it may be found desirable to utilize shorter or longer periods When conditions so dictate within the scope of the invention. It will be observed, however, that in the selection of such time intervals, the rate of consumption ofthe anode shell 11h under a given set of operating conditions, the desirability of maintaining the gap distance D uniform throughout the operative surface and 'the labor costs vinvolved in carrying out the repositioning and refinishing operation are to be taken into consideration.V

While anode 11 is of cylindrical shape having a circular, cross section, others such as hexagonal, octogonal or symmetrically arranged segments or sector cross-sectional shapes or the like, may be cmployedin practicing the invention. Thus, in Fig. 5, a cross-sectional view in outline, like Fig. 2, is shown to illustrate an example of vthat shown-in more detail in Figs. 1 to 4 and described 7 t above for furnace construction 10 and may include similar box framework 212th, passageways 22e, reservoir ZZf, cathode tubes 22m, anode tube 2lb, anode studs 21e, carbon shell 21h, bafiie members 2dr and tapping valve 2S.

In Fig. 6 a cross-sectional view in outline is shown of another modified form of the invention in which furnace construction 30 may be provided with anode 3.1 formed with symmetrically arranged cross-sectional body sectors. Pot portion cathode 32| of said' furnace construction 30 may have a lining 32a formed with an arcuate shaped trough 32d conforming with the curved surface portion of sector of anode 31.

Furnace construction 30` otherwise may be like that shown in more detail in Figs. 1 and 4 as described above for furnace construction 10i and may include box framework 32b, passageways 32e, reservoir 32j, cathode tubes 32m, anode tube Sib, anode studs 31e, carbon shells 31h, baiile members 311' and tapping valve 35.

Said furnace constructions 2t?, 30 and the like, each operate in the same manner as shown and described above for furnace construction iti. The term cylindrical when used to describe the anode in the claims following shall be interpreted in a broad sense to include the configurations of anodes 21 and 31 as well as anode 11.

It is thus seen that there is provided improved furnace constructions and method of operation whereby the several objects of this invention are achieved and which are well adapted 4to meet the conditions of practical use.

As Various possible embodiments might be made of the above invention and as various changes might be made in the embodiments above set forth, it is to be understood that all matters herein set forth or shown in the accompanying drawings are to be interpreted as illustrative and not in a limiting sense.

Having thus described my invention, I claim as new and desire to secure by Letters Patent:

1` In an velectrolytic reduction furnace, an anode mounted for rotation on a longitudinal horizontal axis comprising an elongated tubular metallic electric courrent carrying core having a longitudinal axis forming said axis of rotation, spaced apart metallic electric current distributing studs radiating from said core substantially along the length thereof, a current carrying carboniferous shell in which outer end portions of said studs are embedded, said shell extending radially beyond the free ends of said studs providing an effective terminal surface portion of said anode, and a layer of heat insulating material interposed between said current carrying tubular core and said carboniferous shell, said studs extending through said insulating layer into said carboniferous shell.

v 2. The electrolytic reduction furnace defined in claim l including shafts outwardly projecting in alignment along said axis carried on opposite ends of said tubular core.

3.The electrolytic reduction furnace defined in claim l including lshafts supported at opposite ends of said tubular core outwardly projecting in alignment along said axis,

spaced apart cradle cross arms carrying bearing blocks in which said shafts are journaled for said rotation of said anode, bafiie members extending in parallel relation along the surface of said carboniferous shell interconnecting with said cradle cross arms, and adjustable leveling means electrically insulated from a cathode pot portion and supported in relatively stationary position connecting with said arms and baffle members for selectively varying the anode level to be effective for furnace operational requirements.

4. The electrolytic reduction furnace defined in claim l in which said core has a hollow center and openings at opposite ends thereof to permit circulation of air therethrough for cooling.

5. An electrolytic reduction furnace for extracting aluminum from its ore comprising a cylindrical shaped anode mounted horizontally for axial rotation, said anode having a carboniferous shell with surface portions thereaes-onge of adapted to be alternately immersed in a molten electrolytic bath and removed therefrom for rebuilding by intermittent rotation on said axis, a cathode pot portion having a lining of carboniferous material formed with a trough for retaining said bath, said trough being shaped to conform to the peripheral contour of said immersed surface portion of the anode to provide a uniform gap distance between said anode and cathode, a mid-portion of said trough having through-channels to provide a passage, a reservoir connected with said passage formed in said lining below the level of the trough, and means for connecting said lining in an electric circuit when energizing said furnace.

6. In a method of continuously operating an electrolytic reduction furnace having an anode formed with a current carrying carboniferous shell mounted to turn on a horizontally disposed axis and fitted in operative relation to immerse a rst surface portion of said shell in an electrolytic bath contained in a trough portion of a cathode and to position a second surface portion of said shell accessibly for rebuilding, said first and second anode shell surface portions being of similar predetermined shape and substantially conforming to said cathode trough portion; the steps of operating said furnace with the anode at rest and with said first shell surface portion in register with and at a desired substantially uniform gap distance from said cathode trough portion and immersed in said bath at a required normally high operating temperature for a predetermined time interval until said first shell surface portion is consumed to a desired relatively shallow depth, rotating said anode on said axis through an increment of at least of arc to immerse said second shell surface portion in said bath in register with and at a desired substantially uniform gap distance from said cathode trough portion and to simultaneously position said consumed first shell surface portion accessibly for rebuilding, coating said consumed .first shell surface portion with a carboniferous paste to rebuild said consumed layer forming a refinished surface, partially curing said reiinished surface to semi-hardness by heat radiation from said furnace while said second shell surface portion is being consumed by the operation of the furnace, and thereafter rotating said anode to replace inthe bath in operative position said consumed second shell surface portion by said first refinished partialiy cured portion, while simultaneously frying the latter to a current conducting hardened crust.

7. In the method of operating an electrolytic reduction furnace defined in claim 6, said predetermined time interval for operating the furnace being on the order of eight hours toconsume said shell to a depth on the order of 1A: of an inch.

8. An electrolytic reduction furnace as defined in claim 5 whichincludes an adjustable leveling means supported in a relatively stationary position electrically insulated from said cathode for selectively varying the spaced relation of the anode with respect to the cathode as required for furnace operation. i Y

9. An electrolytic reduction furnace comprising an anode mounted for turning movement'having an axis thereof horizontally disposed and provided with a metallic tubular core extending lengthwise thereof, a current carrying outer shell for said anode supported at a spaced distance from the core and electrically connected therewith, a horizontally disposed pot portion cathode having a current carrying lining formed with a trough lshaped to conform with surface contour portions of said shell, aligned bafiie members spaced to extend longitudinally along parallel sides of said anode, spaced apart cross cradle bars on which said anode is mounted for turning movement spanning opposite ends of said baffle members, and leveling means for said baffle members, cradle bars and anode electrically insulated from said cathode pot portion for selectively raising and lowering the anode to aecomo vary the eiective spaced distance between the anode and cathode as required for surface operation.

10. An electrolytic reduction furnace as defined in claim 9 in which said cathode includes spaced apart current carrying tubular members electrically connected to an underside of said cathode lining o-n which the latter is mounted, and a supporting framework extending along vertically disposed sides, ends and bottom of the cathode pot portion.

11.A An electrolytic reduction furnace, a vhorizontally disposed cathode pot portion comprising a current carrying lining having an elongated trough for retaining material to be subjected to the electrolytic action, said trough being shaped to conform with an elongated section of a anode of cylindrical peripheral contour, a mid-portion of said trough being through-channeled to provide a passage communication with a reservoir formed in said lining below the level of the trough, a framework for supporting said lining having a bottom substantially V-shaped in cross section, longitudinally extending spaced apart beams for supporting said framework bottom,` and spaced apart metallic current carrying tubes longitudinally extending along an underside of said lining between said beams electrically contacting said lining to serve as distributed collectors of current in an electric circuit when said furnace is energized and to carry said lining thereon, each of said tubes being connected with a terminal for tapping a power source.

References Cited in the le of this patent UNITED STATES PATENTS 503,929 Hall Aug. 22, 1893 1,941,387 Camescasse Dec. 26, 1933 2,061,146 Ferrand Nov. 17, 1936 2,680,142 Graybeal June 1, 1954

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US503929 *Aug 22, 1893 Method of producing aluminum
US1941387 *May 28, 1930Dec 26, 1933Magnesium Production Co LtdAnode for fused bath electrolysis
US2061146 *Dec 3, 1934Nov 17, 1936Louis FerrandFurnace for electrolytic purposes
US2680142 *Sep 13, 1951Jun 1, 1954Kaiser Aluminium Chem CorpElectric furnace with horizontally rotating consumable electrode and method and means for replenishing the same
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3110660 *Nov 28, 1960Nov 12, 1963Reynolds Metals CoCathode structure for electrolytic reduction cell
US3170862 *Oct 10, 1961Feb 23, 1965AlusuisseReinforced concrete structure in an electrolytic furnace house for producing aluminum
US4552638 *Nov 13, 1984Nov 12, 1985Aluminum Company Of AmericaNonmetallic conductive electrode, current carrin shaft
US4824543 *Dec 2, 1987Apr 25, 1989Aluminum Company Of AmericaElectrode design for increased current distribution
US5409593 *Dec 3, 1993Apr 25, 1995Sifco Industries, Inc.Method and apparatus for selective electroplating using soluble anodes
U.S. Classification205/389, 204/247.4, 204/212, 204/297.15
International ClassificationC25C3/00, C25C3/08
Cooperative ClassificationC25C3/08
European ClassificationC25C3/08