US3451906A - Respacing of electrodes in electrolytic cells for the production of the halates,perhalates or hypohalites of alkali metals - Google Patents

Description

Filed Oct. 29, 1965 June 24, 1969 w, 5 WEED 3,451,906 'RESPACING OF EL CTRODES IN ELECTROLYTIC CELLS FOR THE PRODUCTION OF THE HALATES. PERHALATES OR HYPOHALITES OF ALKALI METALS Sheet L of 4 JNVENTOR. JOHN W. S. WEED Attorney I June 24, 1969 J. w. s. WEEID RESPACING OF ELECTRODES IN ELECTROLYTIC CELLS F0 PRODUCTION OF THE HALATES, PEHHALATES OR HYPOHALITES OF ALKALI METALS Filed Oct. 2 9, 1965 Sheet R THE -i. or 4 INVENTOR. JOHN w s. WEED BY 2 Attorney,

June 24, 1969 J. w. SHWEED 3,451,906

RESPACING OF ELECTRODES IN ELECTROLYTIC CELLS FOR THE PRODUCTION OF THE HALATES, PERHALATES 0R HYPOHALITES OF ALKALI METALS Filed Oct. 29, 1965 Sheet of 4 F E E m x a m INVENTOR'.Y

JOHN W S. WEED BY fla Attorneyw June 24, 1969 J. w. s. WEED 3,451,906

vRESPYXCING OF ELECTRODES IN ELECTROLYTIC CELLS FOR THE I PRODUCTION OF THE HALATES, PERHALATES OR HYPOHALIT ES OF ALKALI METALS Filed Oct. 29, 1965Sheet 4 of 4 Q Q 7 r if I --19 74 14 n... l H 26 S l i 26 f INVENTOR.

JOHN W S. WEED Aliq ney United States Patent RESPACING OF ELECTRODES IN ELECTROLYTIC CELLS FOR THE PRODUCTION OF THE HAL- ATES, PERHALATES 0R HYPOHALITES OF ALKALI METALS John W. S. Weed, Buckingham, Quebec, Canada, assignor to Electric Reduction Company of Canada Ltd., Toronto, Ontario, Canada Filed Oct. 29, 1965, Ser. No. 505,646 Int. Cl.B01k 3/02 US. Cl. 204--82 Claims ABSTRACT OF THE DISCLOSURE Electrolysis is carried out in an electrolytic cell containing electrodes held in spaced apart relationship with respect to each other by a first set of spacers. After the electrodes are partially consumed they are shifted to another part of the cell or to another cell where the spacers are positioned closer together than the first set of spacers, and electrolysis is carried out using the partially consumed electrodes.

This invention relates to processes for the electrolytic production of the halates, perhalates or hypohalites of alkali metals. More particularly, this invention relates to processes for improving the economy of production of such compounds.

When an alkali metal halide is electrolysed in an electrolytic cell employing consumable electrodes, such as graphite, for example, the electrodes wear away, and eventually they must be replaced.

In a multipolar sodium chlorate cell, for example, there is a definite economic relationship between the cost of the installed graphite electrodes, the total cost of the power supplied, and the total production of chlorate. This relationship is a direct result of the fact that as the graphite electrodes are consumed, the gaps between adjacent electrodes increase, and the power per unit weight of chlorate produced increases. The economic relationship may be expressed as follows:

Cost per pound of chlorate:

Installed graphite eost+ total power cost total production In the past it has been common practice to operate an electrolytic cell for the production of any of the foregoing compounds until the gaps between adjacent electrodes became so large as to materially increase the power cost, and then to discard the electrodes.

- In accordance with this invention, instead of discarding the electrodes after use, they are respaced in the same or another electrolytic cell and used again.

In brief, in accordance with this invention, there is provided a process for producing at least one compound selected from the class consisting of the halates, perhalates and hypohalites of an alkali metal wherein, as in the prior art, an alkali metal halide electrolyte is electrolysed in the electrolysis zone defined between two spaced apart electrodes, at least one of which is consumed during the process, until this one electrode is partially consumed. Thereafter, this partially consumed electrode is positioned with respect to another electrode, which may be the same as the other electrode of the first named two electrodes, such that the spacing (centre to centre) therebetween is less than the spacing that existed between the aforementioned two electrodes. An alkali metal electrolyte then is electrolysed in the electrolysis zone defined between the aforementioned one and another electrodes.

This invention will become more apparent from the following detailed description, taken in conjunction with the appended drawings, in which:

FIGURE 1 is a plan view illustrating electrolytic apparatus for carrying out this invention,

FIGURE 2 is a section taken alongline 22 in FIG- URE 1,

FIGURE 3 is a perspective view of a part of the inside of the electrolytic cell shown in FIGURE 1,

FIGURE 4 illustrates one method of carrying out this invention using only one electrolytic cell and is a section taken along line 4-4 in FIGURE 3,

FIGURE 5 is a view similar to FIGURE 4 illustrating another method for carrying out this invention using only one electrolytic cell, and

FIGURES 6 and 7 are plan views of two electrolytic cells illustrating still another method for carrying out this invention but using two electrolytic cells.

While, for the sake of simplicity, this invention will be described hereinafter in connection with the electrolysis of a brine solution to produce sodium chlorate, it should be understood that the invention is applicable to the electrolytic production generally of a compound selected from the class consisting of the halates, perhalates and hypohalites of an alkali metal.

In addition, it should be appreciated that while this invention will be hereinafter described in connection with bipolar electrolytic cells wherein at least two of the electrodes are monopolar and at least one is bipolar, the electrodes being connected in series electrically, the invention also may be practised with monopolar electrolytic cells wherein there are at least two electrodes and all electrodes are of the monopolar type, all positive electrodes being connected in parallel, and all negative electrodes also being connected in parallel.

Furthermore, while the instant invention will be described hereinafter in connection with electrolytic cells employing graphite electrodes, it is to be understood that other electrodes of a type that are consumed during the operation of the cell may be substituted for the graphite electrodes.

Referring now to FIGURES 1 and 2 there is shown electrolytic apparatus which includes acell tank 10 that is generally circular in plan and which has abottom wall 11 andupstanding side walls 12. Positioned incell tank 10 is anelectrolytic cell 13 that is generally rectangular in plan and which includes a housing having abottom wall 14,upstanding side walls 15 andupstanding end walls 16, the top ofelectrolytic cell 13 being open, as shown. Fixed to and extending through bothside walls 15 are inlet andoutlet tubes 17 and 18 respectively. Means (not shown) are provided for supporting the housing with itsbottom wall 14 spaced abovebottom wall 11 ofcell tank 12. Positioned in the housing ofelectrolytic cell 13 and constituting a part ofelectrolytic cell 13 are a plurality of spaced apart, parallel,graphite electrodes 19 that are spaced inwardly fromside walls 15 and abovebottom wall 14 by means of suitable spacers, which will be described hereinafter in greater detail in connection with FIGURE 3.

The direction of electrolyte flow fromcell tank 10 throughelectrolytic cell 13 and back intocell tank 10 is shown by the arrows in FIGURE 2. Theelectrolyte 20, which, for the production of sodium chlorate, is a brine solution, flows fromcell tank 10 intotubes 17 and thence throughtubes 17 intoelectrolytic cell 13. Electrolysis of the electrolyte takes place in the various electrolysis zones defined betweenadjacent electrodes 19, and the electrolyte then is discharged fromelectrolytic cell 13 throughtubes 18 back tocell tank 10.

Turning now to FIGURE 3, it will be seen that a plurality of spaced apart,parallel grooves 22 are provided inwalls 15 and open into the chamber defined by the housing ofelectrolytic cell 13. These grooves orchannels 22 are perpendicular tobottom wall 14, and extensions thereof are provided at 23 in weirs 21. In addition, as shown in FIGURE 4, grooves orchannels 24 also are provided inbottom wall 14 and open into the chamber defined by the housing ofelectrolytic cell 13.Grooves 24 are parallel to each other and are aligned withgrooves 22 inside walls 15.

Disposed ingrooves 22 areremovable spacers 25 in the form of elongated strips of a suitable material, such as polyvinyl chloride, which, incidentally, also may be used for fabricating cell tank and the housing and tubes ofelectrolytic cell 13. Of course, other suitable materials that are electrical insulators and that are able to resist chemical attack by the electrolyte can be used. It will be seen thatspacers 25 are in tongue and groove relationship withgrooves 22 and project inwardly into the chamber defined by the housing ofelectrolytic cell 13,spacers 25 being at right angles toside Walls 15.

Disposed in tongue and groove relationship ingrooves 24 and upstanding frombottom wall 14 at right angles thereto arespacers 26, which may be made of the same material asspacers 25, and which also are in the form of elongated strips.Spacers 26 extend acrossbottom wall 14 and intogrooves 22, whilespacers 25 sit onspacers 26. Of course,spacers 26 are disposed parallel to each other.

Eachelectrode 19 consists of a group ofgraphite planks 27 that are seated one on top of the other. Thevarious planks 27 of any given electrode are held together by means ofelongated strips 28 of any suitable material, such as glass or polyvinyl chloride, which are disposed ingrooves 29 provided in the top and bottom edges ofplanks 27 and extending the length thereof. The end edges ofplanks 27 are similarly grooved, andspacers 25 extend into these grooves. As shown in FIG-URES 3 and 4,spacers 26 extend into thegrooves 29 in the bottom edges ofbottom planks 27 ofelectrodes 19. It thus will be seen thatspacers 25 and 26 co-operate withelectrodes 19 to hold these electrodes in spaced apart relationship with respect to each other.Electrodes 19 have flat, planar surfaces which are disposed parallel to each other.

Seated in eachgroove 29 in the top edges oftop planks 27 arepartitions 32 of glass or other suitable electrically insulating material that also seat ingrooves 22.Partitions 26 and 32 prevent electrolyte in one unit cell from passing over one of the electrodes of this unit cell into the next adjacent unit cell.

Inlet andoutlet tubes 17 and 18 are shown in FIGURE 3 but, for the sake of simplicity, have not been shown in FIGURE 4. There is one inlet and one outlet tube in each side wall of each unit cell (four tubes per unit cell). As is known in the art, a unit cell consists of two adjacent electrodes and the interelectrode space or electrolysis zone therebetween.

Referring now to FIGURE 4, it will be seen that the spacing between any two adjacent ones of the three electrodes designated 19a, 19b and 190 is the same. It is to be understood, that where herein the term spacing is used, this refers to the centre to centre spacing of the electrodes, i.e., the spacing ofpartitions 26 on a centre to centre basis. It also will be noted that the spacing between any two adjacent ones of the three electrodes designated 19d, 19c and 19 is the same. However, the spacing between any two adjacent ones ofelectrodes 19a, 19b and 190 is greater than the spacing between any two adjacent electrodes ofelectrodes 19a, 19a and 19f, but, in all cases theinterelectrode gaps 33, i.e., the distance between adjacent surfaces of adjacent electrodes, is the same.

The only difference between the apparatus shown in FIGURE 4 and that shown in FIGURE 5 is that spacers and 26 are formed integral withside walls 15 andbottom wall 14 respectively rather than being removably 4 positioned in grooves in these walls. Again, as in the case of FIGURE 4, the spacing A between any two adjacent electrodes of the group of electrodes within the group marked B is the same. The spacing C between any two adjacent electrodes of the group of electrodes marked D also is the same, but C is less than A. In all cases, however, theinterelectrode gaps 33 are the same.

Theelectrodes 19 shown in FIGURES 4 and 5 all are within the housing ofelectrolytic cell 13 and constitute a part ofelectrolytic cell 13. Theelectrodes 19 are shown as they would be before use of the cell to produce sodium chlorate by electrolysis of brine is commenced.

As is known in the art, the end electrodes of the electrodes of the electrolytic cell are connected to the positive and negative terminals of a rectifier (not shown) and, in practising this invention, electrolyte 20 (brine) is electrolysed in the electrolysis zones between the facing surfaces of adjacent electrodes, the electrolyte from the various unit cells being discharged throughtubes 18 back intocell tank 10 where a chemical reaction producing sodium chlorate takes place. The electrolyte recirculates and passes into the various electrolysis Zones throughtubes 17, and the electrolysis process is repeated. During this process the graphite electrodes are consumed. In accordance with this invention, after thegraphite electrodes 19a, 19b and 19c have been partially consumed, they are removed from the electrolytic cell, along withelectrodes 19d, 19:: and 19f, and the partially consumedelectrodes 19a, 19b and are substituted for or replaceelectrodes 19d, 19a and 19 These latter electrodes may be discarded or may be substituted for other electrodes. New electrodes of the same size and type aselectrodes 19a, 19b and 190 are provided to replaceelectrodes 19a, 19b and 190. Electrolysis ofelectrolyte 20 then may be continued.

As a more specific example,electrodes 19a, 19b and 190 initially may be 1 inch in thickness, whileelectrodes 19d, 19a and 19 initially may be inch in thickness. The interelectrode gaps may be inch. Afterelectrodes 19a, 19b and 190 have been consumed to the point that they are inch in thickness, they are used to replaceelectrodes 19d, 19c and 19Electrodes 19d, 19e and 19 need not be discarded at this point but could be used to replace other electrodes that are thinner thanelectrodes 19d, 19c and 19], in the same way aselectrodes 19a to 190 are used to replaceelectrodes 19d to 19f. Generally, however, electrodes should be discarded after they have been consumed to the point where they are only about inch in thickness, so that there is a limit to the number of times that any given electrode can be respaced.

It should be noted that it is not essential that allinterelectrode gaps 33 be the same, but this is desirable.

Those skilled inthe art will appreciate that by respacing the electrodes as outlined hereinbefore, considerable economy eifected insofar as power cost is concerned, because the cost of power increases as the interelectrode gap increases, so that if a 1-inch electrode were used in an electrolytic cell without respacing the electrode and until the electrode had been consumed to the extent that it was only about A inch in thickness, the interelectrode gap between this electrode and its adjacent electrodes would have increased very measurably, as would have power cost.

It is not necessary to practice this invention by respacing electrodes within one electrolytic cell. Thus, as shown in FIGURES 6 and 7, twoelectrolytic cells 13a and 13b of the type hereinbefore described are provided, but the spacing betweenadjacent electrodes 19 inelectrolytic cell 13a is greater than the spacing betweenadjacent electrodes 19 in electrolytic cell 1311. It may be considered that electrode assemblies employing electrodes like 19a, 19b and 190 of FIGURE 4 are used inelectrolytic cell 13a, while electrode assemblies employing electrodes like 19d, 19c and 19 of FIGURE 4 are used inelectrolytic cell 13b. Both electrolytic cells are operated to produce the desired compound by electrolytic action. Both cells need not produce the same compound, however. Afterelectrodes 19 inelectrolytic cell 13a have been partially consumed, they are removed from this cell and are used to replaceelectrodes 19 inelectrolytic cell 13b. New 5electrodes 19 of the same size and type as wereelectrodes 19 incell 13a initially are placed in this cell, while partially consumedelectrodes 19 fromcell 13b may be discarded or, depending on their thickness, used in another electrolytic cell wherein the spacing between adjacent electrodes is even less than the spacing between adjacent electrodes incell 13b. Electrolysis of an electrolyte incells 13a and 13b then is continued.

While preferred embodiments of this invention have been disclosed herein, those skilled in the art will appreciate that changes and modifications may be made therein without departing from the spirit and scope of this invention as defined in the appended claims.

What I claim as my invention is:

1. A process for the electrolytic production of at least one compound selected from the class consisting of the halates, perhalates and hypohalites of an alkali metal which comprises; providing a first electrolytic cell comprising a housing having a bottom wall and side walls defining a chamber, a plurality of spaced apart spacers extending into said chamber from said Walls, and a plurality of electrodes located in said chamber and cooperating with and held in spaced apart relationship with respect to each other by said spacers, said electrodes defining therebetween an electrolysis zone, at least one of said electrodes being of a type that is consumed during use of said electrolytic cell; providing a second electrolytic cell comprising a housing having a bottom Wall and side walls defining a chamber, a plurality of spaced apart spacers extending into said chamber of said second electrolytic cell from said walls thereof and adapted to co-operate with electrodes located in said chamber of said second electrolytic cell and hold the electrodes in spaced apart relationship with respect to each other, the spacing between adjacent ones of the spacers of said second electrolytic cell being less than the spacing between adjacent ones of the spacers of said first electrolytic cell; electrolysing an alkali metal halide electrolyte in said first electrolytic cell until the consumable electrode is partially consumed; subsequently removing the partially consumed electrode from said first electrolytic cell; placing said partially consumed electrode in said chamber of said second electrolytic cell along with other electrodes, the electrodes in said chamber of said second electrolytic cell co-operating with and being held in spaced apart relationship by said spacers of said second electrolytic cell and being spaced closer together than said electrodes in said chamber of said first electrolytic cell; and electrolysing an alkali metal halide electrolyte in said second electrolytic cell.

2. A process according to claim 1 wherein each interelectrode gap between said one electrode and each adjacent electrode thereto in said first electrolytic cell prior to electrolysing of said electrolyte in said first electrolytic cell is the same as each interelectrode gap between said partially consumed electrode and each adjacent electrode thereto in said second electrolytic cell prior to electrolysing of said electrolyte in said second electrolytic cell.

3. A process for the electrolytic production of at least one compound selected from the class consisting of the halates, perhalates and hypohalites of a alkali metal which comprises; providing an electrolytic cell comprising a housing having a bottom wall and side walls defining a chamber, a plurality of spaced apart spacers extending into said chamber from said walls, and a plurality of electrodes located in said chamber and co-operating with and held in spaced apart relationship with respect to each other by said spacers, first ones of said spacers in one part of said electrolytic cell being positioned closer together than second ones of siad spacers in another part of said electrolytic cell, said electrodes defining therebetween an electrolysis zone, at least one of said electrodes held by one of said second spacers being of a type that is consumed during use of said electrolytic cell; electrolysing an alkali metal halide electrolyte in said electrolytic cell until the consumable electrode is partially consumed; subsequently removing the partially consumed electrode and one of said electrodes held by one of said first spacers; replacing said last-mentioned electrode with said partially consumed electrode; replacing said partially consumed electrode with another electrode; and subsequently electrolysing an alkali metal halide electrolyte in said electrolytic cell.

4. A process according tocaim 3 wherein said partially consumed electrode is replaced with an electrode of substantially the same size and type as was said consumable electrode before use of said electrolytic cell.

5. A process according toclaim 3 wherein each interelectrode gap between said one electrode and each adjacent electrode thereto held by said second spacers prior to the first electrolysing step is the same as each interelectrode gap between said partially consumed electrode and each adjacent electrode thereto held by said first spacers prior to the second electrolysing step.

References Cited UNITED STATES PATENTS 566,673 8/ 1896 Fielding 204-268 633,272 9/ 1899 Parker 2.04- 651,849 6/ 1900 Haas 204-268 685,274 10/ 1901 Haas 204-268 2,480,474 8/ 1949 Johnson 204-26'8 XR 3,375,184 3/ 1968 Giacopelli 2.0 4225 JOHN H. MACK, Primary Examiner. D. R. JORDAN, Assistant Examiner.

US. Cl. X.R. 204-95, 269, 275

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