US951229A

US951229A - Electrolytic cell.

Info

Publication number: US951229A
Application number: US46784708A
Authority: US
Inventors: Jasper Whiting
Original assignee: WHITING Co
Current assignee: WHITING Co
Priority date: 1908-12-16
Filing date: 1908-12-16
Publication date: 1910-03-08
Anticipated expiration: 1927-03-08

Description

` J. WHITING. BLEGTROLYTIG CELL. APPLIOATIGN FILED DBO. 16, -190s.

Patented Mar. 8, 1910.

a SHEETS-SHEET 1l J; WRITING. ELEGTROLYTIG CELL.

APPLICATION FILED DEO. i8, 1908.

' Patented Mar.8,1910.

3 SHEETS-SHEET 2.

UNITED STATES PATENT OFFICE.

JASPER WHITING, OF BOSTON, MASSACHUSETTS, ASSIGNOR TO WHITING- COM- PANY, 0F BOSTON, MASSACHUSETTS, A CORPORATION OF MAINE.

ELECTROLYTIC CELL.

To all whom lit may concern.'

Be itknown that I. JASPER WHiTiNc, a citizen of the United States, residing at Boston, in the county of'Suolk and State of .B/lassachusetts, have invented certain new 4ratus employing as cathode a body ofliquid metal or alloy. In operations of this character it has been usual heretofore 'to vmaintain a substantially continuous circulation of the cathode, but this practice has proven objectionable by reason of the tendency of the electrolytically separated metal, as sodium, to become oxidized and to renter into solution in the decomposing compartment. Forv example, in the production of caustic soda by electrolysis of aqueous solutions of sodium chlorid in presence of a mercury cathode, the sodium amalgam tends to collect at the surface of the cathode and its removal tothe oxidizing compartment is only incompletely effected bv the flow of the und rlying body of mercury; the sodium of theamalgam is therefore subject to oxidation by the electrolyte undergoin decomposition, resulting in a reduced e ciency of operation. J

In my prior patent No. 877,537, granted January'28, 1908, I have-described a'method of electrolyzing salts wherein a cathode of liquid metal or alloy is maintained in a quiescent state during the period of electrodeposition therein of an alkali or other metal, the cathode being eriodically co-nveyed from the decomposing compartment to a suitable oxidizing compartment, and returned to said decomposing compartment,

the iow of the electric current beingpreferably maintained without interruption by the provision of a4 plurality of bodies of the cathode metal adapted to lbe conveyed in succession to the oxidizing compartment or v compartments. As described in said patent,-

the contents of the decomposing and oxidizing compartments are in balanced relation, and the metal or alloy which is discharged periodically from the decomposing compartment is conveyed to a pump or equivalent device by means of which it is elevated and discharged into the oxidizing compartment, the denuded metal flowing thence by grav- Specication of Letters Patent.

Application led December 16, 1968. Serial No. 467,847.

Patented Mar. 8, 1910.

ity to the decomposing compartment where its contents of alkali metal is restored. The present invention is an electrolytic 'cell having decomposing and oxidizing compartments adapted to contain liquid metal, and provided with means operating at pre-- determined intervals for transferring said metal from the decomposing to the oxidizing compartment. This cell may be of the character described in my priorpatent above referred to, wherein the contents of the def composing and oxidizing compartments are in balanced relation and the amalgamis elevated to the oxidizing compartment and permitted. to return thence by gravity to the decomposing compartment. I prefer however to provideamodified form of appa;- ratus wherein the liquid metal is during the charging period mechanically separated from the contents of the oxidizing compartment, and is permited'to flow thereinto by gravity at the close of such period, this construction securing several important advantages as hereinafter set forth.

For a full understanding of the invention the same will be described by reference to the production of caustic soda by the electrolytic decomposition of an aqueous solution of sodium chlorid in the presence of a" cathode of mercury.

A preferred form of apparatus is illus Y trated 'in the accompanying drawings where- Figure 1 is a longitudinal section on line 1-1 of Fig. 3; Fig. 2 is a side elevation of the apparatus; Fig. 3 is a plan'view of the same; Fig. 4 is a transverse vertical section on the broken. line 4 -4 of Fig.v 3; and Fig.

5 is afragmentary vertical sectional View` showing a preferred form of elevating de,`

vice or pump for the mercury.

Referring to thedrawings l represents a 'body ofJ cement, concrete or other suitable formed in the bottom of the decomposing compartment 2: it will be understood however that a single body of mercury or any desired number of bodies may beprovidedl in the decomposing compartment. These basins g may be lined with glass, slate or earthenware -by means of which t 5 and are separated from each other by low partitions 6 set in the cement base and extending above the normal surface of the mercuryv cathode, the arrangement providing a common body of electrolyte above the several separated bodies of mercury.' 7 is a similar partition disposed transversely of the basins 4 and nearl one end thereof in such manner as to provide an equalizing channel 8 from which the mercury may flow to the several basins, this equalizing channel 'being supplied with mercury from a distributing conduit 9 which receives the denuded -metal from the oxidizing compartment. Above each basin is disposed-an anode or anodes 10, which may be vertically slotted as indicated at 11 to permit the escape of chlorin. These anodes are usually of graphite and are carried at one end .by a ledge 12 integral `with the cell body, and at the other by the partition 7 The anodes preferably extend over the mercury in the equalizing channel `as shown in such manner as to constitute the mercury therein a part of the active cathode, whereby the capacity of the cell is increased to a corresponding extent. The several anodes are electrically connected in circuit through graphite leads 13 extending upwardly through the cover 14 of the decomposing compartment. The cover 14 is removable together with the anodes, this larrangement permitting the ready opening of the cell for inspection, cleaning or the repair or replacement of parts.

Centrally disposed in the bottom of each basin 4 is a longitudinal slot or channel 15, the mercury in which is in electrical contact with suitable conductors 16 which are embedded in the body 1 and are connected to the cathode bus bars 17. The slots 15 inoline downwardly to the discharge end of the cell, and communicate at their lower ends with conduits 18 through which the amalgam may be discharged into the oxidizing compartment 3. At the bottom of each slot are shown a plurality of wells 15a adapted to retain small volumes of'mercury which serve to protect the metallic conducting plates 16 and to establish electrical contact between them and the overlying amalgam. Each slot terminates at its lower end in a pocket 15b, the construction being such as to permit the mercury to be discharged from the cell or compartment with substantial comleteness. -Each conduit 18 is provided at its discharge end with a` weighted valve v19 normally closing the same but adapted to be opened at desired intervals by the movement o levers 20, actuated by cams 21, carried by a rotary shaft 22. 'Ihe valves 19 are guided to their seats by Vdownward projections 19a. As illustrated, they are suspended by chains 19", and an adjustin screw 19 is provided lie lift of the valve may be` varied as desired. It will be understood however that the invention is not restricted to the particular means illustrated for operating the valves at the desired or predeterminedv intervals. l/Vhen the valves 19 are opened the mercury or amalgam in the rcspective basins of the decomposing compartment flows by graxf'ity upon the inclined surfaces 23 (Figs. 3 and 4) and thence through channels 24 to the oxidizing compartment 3. In the particular form of apparatus illustrated, the oxidizing compariment comprises a series of wide shallow channels 25, 26, 27 disposed at successively lower levels and separated by partitions 28 so arranged that the amalgam is directed in a tortuous path as indicated by the arrows through the several channels, the denuded mercury flowing finally to the sump 2S) (Fig. 5). It is then elevated by a rotaryY disk pump 30 and returned by conduit 31 (Figs. 2, 3) to the distributing conduit S), passing thence to the equalizing channel 8 andthe proper basin of the decomposing compartment. Ns indicated in Figs. 1 and 3 the bottom of each of the channels 25, 2G, 27 of the oxidizing compartment is constituted by a carbon or graphite slab 32, having integral members 33 projecting upwardl into contact with the water or oxidizing electrolyte, the members 33 being disposed to permit a ready flow of the amalgam while providing a maximum contact therewith. The oxidizing compartment is supplied with water, the caustic soda solution escaping through an outflow 34.

It is important that the denuded mercury should be freed from adhering or mechanically conveyed caustic soda solution before rentering the decomposing compartment. In the present construction this may he accomplished by the provision of traps lor seals of any ordinary type in the conduits 31 and 9. Thus I have illustrated in Fig. 2 a trap or seal 35 arranged in connection with the discharge line of the pump 30 and serving to retain the supernatant liquid while permitting the flow of the mercury. A

similar arrangement comprising a partition extending below the surface of the mercury in distributing conduit 9 is indicated at in Fig. 3. If desired the mercury may readily be washed and thereby thoroughly freed from alkaline constituents bythe introduction of water into the conduit 31 at a point conduits 41 as the pockets are brought successively into proper relation to a trough 42, leading to the conduit 31. As shown, the pump 30 is mounted on a shaft 43 carrying a sprocket 44, driven by a chain 45 from a sprocket 46 on a shaft 47 having a clutch connection 48 with a power shaft. This apparatus for elevating the mercury 1s found to operate without such agitation of the metal as would result in its subdivision into globules with consequent danger of loss, and is claimed in my co-pending application, Ser. ilo. 467,848, filed December 16, 1908.

I prefer to provide in connectionwith the cell an intermittently operating device forsupplying the electrolyte to the decomposing compartment, this device being automatic in character and permitting the electrolyte to flow into the several basins of the decomposing compartment only while the mercury or amalgam isabsent therefrom or substantially so. As herein illustrated this feed de vice comprises a plurality of receptacles 49 disposed in the cover of the cell above the respective basins 4, and interconnected 4by open channels 50. From the bottom of each receptacle 49 a tube 51 extends downwardly below the normal surface of the mercury in the basins 4 in such manner as to be sealed thereby. Electrolyte is supplied to one of the receptacles 49 and. conveyed' by the equalizing channels 50 to each of the others, any excess being permitted to return to the circulating system, or if desired to flow continuously into the decomposing compartment as through conduit 52. So long as the several basins 4 contain suticient mercury to seal the lower ends of the vdischarge tubes 51, the electrolyte is prevented from flowing therethrough, but when the mercury is discharged from any basin into the oxidizing compartment this seal is broken and a quantity of electrolyte corresponding approximately to the capacity of the receptacle 49 'flows into the decomposing compartment.

By this arrangement the fresh electrolyte is introduced at the bottom of the cell beneath the body of partially spent and consequently lighter electrolyte therein, and distributes itself beneath the latter, therebyA providing a body of substantially saturated electrolyte at the precise point where the electrolytic decomposition is most active. Furthermore by the arrangement described this introduction of electrolyte occurs while there is no amalgam in the cell, and is therefore without tendency to agitate the amalgam or to,

re-dissolve the alkali metal.

In the operation of the apparatus described thevmercury in the several basins 4 vbeneath a common body of electrolyte in the decomposing compartment 2 remains in that is to say the period during which the sodium is being electrically deposited, and

is therefore under the' most favorable condithe conduit 18 between the decomposing andA oxidizing compartments, flows rapidly byv gravity but without serious agitation to the ,oxidizing compartment 3, traverses the same and is thereby denuded of its alkali metal. The pure mercury is then conveyed by pump 3() to the conduit 31 and thence through lconduit 9 and equalizing channel 8 to the decomposing compartment, iowing as will be understood into an empty or discharged basin, in preference to one containing mercury. By the slow rotation of the shaft 22 the next cam 21 will after an appropriate interval be brought intol position to raise the valve 19 of the basin next in series, the operation continuing in such manner that the.

mercury in the several basins 4 is discharged l in rotation and at proper intervals, denuded of its alkali metal, and returned to the decomposing' compartment. As the amalgam is discharged from each basin a body of fresh electrolyte is introduced through the tube 51 -beneaththe body of partially spent electrolyte therein, thereby maintaining the required degree of sat-uration of the electrolyte. lVhile the liquid cathode is maintained during the charging period in a state of rest, it will be observed that during the oxidizing period it is caused to iow in contact with carbon surfaces andment instead of being elevated to the oxidiz-v ing compartment and beingn permitted to flow by gravityjtherefrom vvvto the decomposing compartment. Among such advantages arethefollowing *(1) During the charging period the mercury and superposed electrolyte in the decomposing compartment is mechanically separated` from that'in the oxidizing lcompartment instead of being in balanced relation therewith, whereby .it is not subject to fluctuation inlevel or .variation in quantity due V1to the changes in the relative density of the electrolytes or in the pressure of they evolved gases: therefore more nearly constant current conditions may '-be maintained and the general operation of the cell impioved. (2) There is less liability to the conveyance of caustic soda. or other alkaline constituents from the oxidizing to the decomposing compartment, the flow of the denuded mercury to the decomposing compartment being tortuous, involving passage through a pump or elevating device and providing opportunities for further purifying operations to be performed upon it. (3) The arrangement permits the equalizing channel for the mercury to be placed Within the decomposing compartment, thereby rendering the mercury in this channel availablefor use as a part of the cathode and correspondinglyincreasing the cell capacity. (4) The method provides for the pumping of pure mercury instead of amalgam, this being advantageous as avoiding all tendency to the formation of incrustations outside of the oxidizing chamber. '(5) i The construction is such as to'peimit the mercury to be discharged with substantial completeness from the decomposing cell or compartment. (6) The cell is more compact,

more economical as regards the use of inercury, and of simpler and less expensive construction.

Il claim l. A decomposing cell having a liquid metal cathode, an outlet for said cathode,

controlling means for said outlet, and means operating at predetermined intervals for actuating said controlling means.

2. A decomposing cell having a liquid metal cathode, an oxidizing cell, a conduit for liquid metal extending between said cells, controlling means in said conduit, and means operating at predetermined intervals for actuating said controlling means.

3. A decomposing cell having a liquid metal cathode, an oxidizing cell, a conduit for conveying" liquid metal from the decoinposing to the oxidizing cell, controlling means in said conduit. means operating at predetermined intervals foi;i actuating said controlling means, and means for returning the liquid metal tothe decomposing cell.

4. An eleetrolytic cell having decompos- 'ing and oxidizing compartments, a conduit for mercury extending between said .conipartinents, controlling means in said iconduit, and means operating at. predeterminedl intervals for actuating said controlling means. f

5. A decomposing cell having a pluralit7 of bodies of liquid metal constituting the cathode, and means operating in conjunction with each of said'bodies for Withdrawing the same from the cell at predetermined intervals.

6. In an electrolytic cell, a decomposing compartment containing a plurality of bodies of liquid metal constituting the cathode,

an oxidizing compartment, means operating in conjunction with each of said bodies for transferring the same at predetermined intervals to the oxidizing compartment, andineans for returning the liquid metal from the oxidizing to the decomposing compartmetal between said compartments.

9. In an electrolytie cell, a decomposing compartment containing a quiescent body of `liquid metal constituting the cathode, an

oxidizing compartment, means for transferring said body to the oxidizing coinpartment at predetermined intervals, and means for returning the denuded metal to the decomposing compartment.

10. In an electrolytic cell, a decoin osing compartment containing a plurality o quiescent bodies of liquid metal constituting the cathode, an oxidizing compartment, means for transferring said bodiesl successively to the oxidizing compartment at predetermined intervals, and means for returning the deiiuded metal to the decomposing compartment.

l1.A In an electrolytic cell, a decomposing compartment containing a plurality of quiesent bodies of liquid metal constituting the cathode, an oxidizing compartment, means for transferring said bodies successively to the oxidizing compartment, and means for returning the denuded metal to the. decoinposing compartment. i U

12. In an electrolytie cell, a decomposing compartment containing a plurality of shallow receptacles for liquid lmetal under a common body of electrolyte, an outlet for each receptacle, and controlling means for each outlet.

13. In an electrolytic cell, a decomposing iic compartment containing a plurality of shal- `said decomposing compartment, means operating at predetermined intervals for 4permitting said body to iiow from the decomposing to the oxidizing compartment, and meansv for returning the denuded metal to the decomposing compartment.

15. In an electrolytic cell, a decomposing compartment containing a body of liquid metal constituting the cathode, an oxidizing.

compartment at a lower level than said decomposing compartment, means operating at predetermined intervals for permitting said body to flow from the decomposing to the oxidizing compartment, and means operating continuously for returning tlie denuded metal to the decomposing compartment.

16. In an electrolyticcell, a decomposing Vcompartment containing a body of liquid metal constituting the cathode, an oxidiz` ing compartment at a lower level than said decomposing compartment, a valve between said compartments for control-ling the liow of liquid metal, means operating at predetermined intervals for actuating said con'- trolling means, and means for returning the denuded metal to the decomposing coinpartment.

18. In an electrolytic cell, a decomposing` compartment containing a body of liquid metal constituting the cathode, an oxidizing compartment at a lower level than said decomposing compartment, a valve between said compartments for controlling the flow of liquid metal, meansoperating at predetermined intervals for actuating said valve, and means for returning the denuded metal Vto the decomposing compartment.

19. In an electrolytic cell, a decomposing compartment containin a plurality of bodies of liquid meta constituting the cathode, an oxidizin' compartment at a lower level'than said decomposing compartment, means operating at predetermined intervals for permitting said bodies to fiow successively from the decomposing to the oxidizing compartment, and means for returning the denuded metalto the decomposing compartment. 5

20; In an electrolytic cell, a decomposing compartment containing a plurality of 'bodies of liquid metal constituting the cathode, an oxidizing compartment at a lower level than said composing compartment, means operating at predetermined intervals for ermitting saidbodies to How successively` rom the decomposing to the oxidizing compartment, and means operating continuously for returning the denuded metal tol tlie decomposing compartcment.

A `21. In an electrolytic cell, a decomposing compartment containing a. plurality of independent bodies of liquid metal constituting the cathode and underlying a common body of electrolyte, an oxidizing compartment at a lower 'level than said decomposing compartment, means for controlling the flow of li uid metal between said compartments, an means for returning the deiiuded metal tothe decomposing compartment.

22. In an electrolytic cell, a decomposing' compartment containing a plurality lof shallow receptacles for liquid. metal under a common body of electrolyte, an outlet for each receptacle, controlling means for each outlet, and an oxidizing compartment below said receptacles and in position to receive the metal therefrom. i

23. In an electrcolytic cell, a decomposing compartment containing a plurality of shallow receptacle for liquid metal,` an outlet for each receptacle, controlling means. for each outletmechanism operating in conjunction with said controlling means for discharging the liquid meta-l from said receptacles in succession, and an oxidizing compartment below said receptacles and in n position to receive the metal therefrom.

24. In an electrolytic cell, a decomposing 4compartment comprising a plurality of bodiesof liquid metal constituting a catliode, an equalizing channel containing liquid metal in electrical connection with said bodies, and an anode above said bodies and equalizing channel.

v25. In an electrolytic cell the combination of a liquid metal cathode, and an intermittently operating feed device for admitting electrolyte to said cell, said feed device controlled by said cathode.

26. In an electrolytic cell, the combination of a liquid metal cathode, and a feed device for electrolyte having a discharge opening below the normal surface of said cathode. 27. Inan electrolytic cell the combination of a liquid metal cathode, means operating at predetermined intervals for discharging the same from the cell,` and a feed device for electrolytehaving ay discharge opening below the normal surface of said cathode.

28. In an electrolytic cell theA combination of a liquid metal cathode, meansoperating at predetermined intervals for discharging the same from the cell, and an intermittently operating feed device for supplying electrolyte to said cell, said feed device controlled by said cathode.

29. In an electrolytie cell the combination of a liquid metal cathode means for periodically removing said cathode from the cell and'returnng 1t thereto, and a feed4 device constructed and arranged to admit electrolyte to the cell While the 'cathode is removed therefrom.

JASPER WHITING.

Wtnesses:l

JoHN L. PALFREY, BERTHA S. CHASE.