US518786A - Diaphbagm-fob electrolytic cells - Google Patents

Diaphbagm-fob electrolytic cells Download PDF

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US518786A
US518786A US518786DA US518786A US 518786 A US518786 A US 518786A US 518786D A US518786D A US 518786DA US 518786 A US518786 A US 518786A
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diaphragm
cell
frame
liquid
sheet
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/17Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
    • C25B9/19Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • C02F2201/46115Electrolytic cell with membranes or diaphragms

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  • the difficulty is due to the fact that a diaphragm which is impervious to the passage of the liquids and will therefore keep them wholly separate is apt to interpose a high resistance to the passage of the current.
  • the thing to be desired is a durable diaphragm which will perfectly separate the contents of the cell and will at the same time be of very low resistance.
  • Vegetable parchment has been employed and aifords an excellent diaphragm both as to non-porosity and low resistance but it lacks durability in a cell in which a corrosive substance like chlorine is evolved and will go to pieces in a short time.
  • Figure l is a vertical section of a cell or containing vessel showing my improved diaphragm.
  • Fig. 2 shows the upper portion of the central frame hereinafter referred to.
  • Fig. 3 is a perspective of a portion of the side frame in which the carbon electrode is supported.
  • Fig. 4 is a similar view of the other side frame in which the negative electrode is supported.
  • Fig. 5 is a detail on a smaller scale, which is hereinafter referred to.
  • the outer containing vessel or cell is shown at A, and may be of any well-known shape or construction.
  • the brine or solution which is to be decomposed is contained within this cell, the level of the liquid therein being indicated at a.
  • An overflow isshown at b which serves to. prevent the liquid in the positive electrode compartment of the cell from rising above the level indicated. If required a similar overflow may be provided in the negative electrode compartment, as indicated by dotted lines in Fig. 1.
  • a frame, which I have termed the central frame is shown at c and is constructed of suitable material as lead, for example, and made to fit the interior of the cell A closely.
  • the cross piece d at the top of the frame 0 is joined to the upright portions level of which is somewhat higher than that of the frame somewhatbelow the top thereof as shownFig. 2 so as to leavethe uprights projecting above the cross piece.
  • a series of holes 6 which pass vertically through the cross piece at are made therein. frainecare made true so that a diaphragm or layer of material may be securely clamped thereon said layer or diaphragm being secured IOO The sides of the the passage of the current.
  • the layer f is secured in place by clamping it betweenthe frame a and a side frame g which supports the positive or carbon electrode 71..
  • a series of rods are placed in the frame g crosswise thereof and adjacent the layer or sheet f.
  • the rods 7c are preferably secured in place by being laid in aslot or recess provided ateach end of each rod in the uprightportion of the side frame g as shown Fig. 3.
  • the rods it serve to prevent the asbestus layer f from bulging toward the carbon electrode.
  • On the other side of the frame 0 I placeanother side frame Z shown Fig. 4E between which and the frame 0 is clamped a layer ,orsheet of parchment m or a material having the qualities of parchment and ofwhich parchment is the type.
  • the negative electrode which may be a sheet of iron netting is preferably secured adjacent theparchment sheetand serves to prevent said sheet from bulging toward the negative side of the cell.
  • the positive wire is indicated at qand the negative wire at 0*.
  • the diaphragm proper that is the parchment layer m is separated from the layer or sheet of asbestos f by the thickness of the frame a and this may bevaried as desired without departing from my invention.
  • the space betweenthe layers or sheets m and f is provided with brine which is supplied as desired to .the space shown at s Fig. 1 directly above the cross piece cl of the central frame 0. This brine passes down through the holes 6 into the space below the said cross piece at and between the layers m and f.
  • the level of the liquid in the intermediate space between said layers is maintained at a higher level than the level a of the liquid outside said space.
  • This causes a flow of the liquid outwardly through the pervious asbestos layer from the space between the layers m f toward the positive electrode side of the cell and thus serves to prevent the chlorine or any of the liquid containing chlorine from reaching the parchment diaphragm m.
  • the parchment is quite durable unless attacked by the chlorine its life isin this way prolonged and its efiectiveness secured.
  • As the layer of asbestos f is not attacked by chlorine its full efficiency is also obtained and a diaphragm of great durability and efficiency is the result.
  • the diaphragm or non-poroussheet m from their action the negative electrode may be removed somewhat from the I said diaphragm-and a pervious sheet similar to the sheet f may be placed on the negativesideof thesheet m, ina manner similar to that in which it is shown as arranged on the positive side in the drawings and the supply of the solution for the negative compartment maybe caused to take place through this pervious sheet.
  • the arrangement shown in Fig. 1 is for use in caseswhere the products of decomposition which are liberated at the negative electrode are notsuch aswill attack theparchmentsheet.
  • the central frame a maybe made by cutting it from heavy sheets of lead.
  • the holes 6 in the cross bar (1 of said frame not onlyserve for the admission of the solution but also for .the escape of any bubbles of gas which may be liberated in the inter-diaphragm space.
  • the negative electrode frame Z is preferably of slate but it may be of high qualitystone ware or of glass.
  • the rods 70 are also preferably of glass.
  • the device employed for clamping the frames together is not shown but any well known clamp may be employed.
  • the frames employed for supporting the diaphragm as also the pervious sheet or sheets may be varied as will be obvious in form and construction without departing from my invention, the important feature of which is the separation of the diaphragm proper from'the corrosive product by the interposition of a pervious sheet and fresh liquid, the latter flowing away from the diaphragm.
  • An electrolytic cell having in combination with the diaphragm thereof a pervious sheet or layer interposed between said diaphragm and the electrode of the cell, and separated from said diaphragm by a space forming a chamber containing liquid under greater relative pressure than the liquid in the adjacent compartment of thecell, whereby the movement of the liquid in the cell due to the said greater pressure will be from said diaphragm and through the pervious sheet or layer, substantially as set forth.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electrodes For Compound Or Non-Metal Manufacture (AREA)

Description

(No Model.)
B. A. LE SU EUR. DIAPHRAGM FOR ELEGTROLYTIU CELLS.
N0.518,786. U 4 PatentedApr.24,1894.
UNITED STATES PATENT OFFICE.
ERNEST ARTHUR LE SUEUR, OF OTTAWA, CANADA.
DIAPHRAGM FOR ELECTROLYTIC' CELLS.
SPECIFICATION forming part of Letters Patent No. 518,786, dated April 24, 1894.
' Application filed August 29,1892. Serial No. 444,488. (No model.)
T on whom it may concern:
Be it known that I, ERNEST ARTHUR Ln SUEUR, a subject of the Queen of Great Britain,residing at Ottawa, in the Province of Ontario, Dominion of Canada, have invented certain new and useful Improvements in Diaphragms for Electrolytic Cells, of which the following is a specification, reference being had therein to the accompanying drawings.
In an electrical apparatus designed for the decomposition of common salt and similar chemical substances it is necessary to interpose a diaphragm between the positive and negative electrodes. The office of the diaphragm is to keep the products of decom'po-j sition in their respective portions of the cell. If some such device were not employed the two would mix and besides depreciating the purity of the products of decomposition, the working of the apparatus would be seriously affected, from the fact that the current would expend itself in decomposing the secondary products formed by the combination of soda and chlorine instead of expending its energy in decomposing the brine proper. Great difficulty has been experienced in obtaining suitable material and arrangements of the same for the diaphragms insuch cells. The difficulty is due to the fact that a diaphragm which is impervious to the passage of the liquids and will therefore keep them wholly separate is apt to interpose a high resistance to the passage of the current. The thing to be desired is a durable diaphragm which will perfectly separate the contents of the cell and will at the same time be of very low resistance. Vegetable parchment has been employed and aifords an excellent diaphragm both as to non-porosity and low resistance but it lacks durability in a cell in which a corrosive substance like chlorine is evolved and will go to pieces in a short time. Asbestus on the other hand will resist the action of the chlorine, but if used in a sheet thin enough to be of low resistancgthe liquid will pass through it too freely, whileiif it is made thick enough to prevent the passing of the produce a diaphragm which shall obviate these objections and by the use of which the A diffusion of the liquid contents of the cell may be prevented while the resistance is maintained at a minimum, and it consists in a diaphragm composed of two layers or sheets of material separated by a mass of liquid, the
of the level of the liquid in the cell, all as more particularly hereinafter set forth and as is pointed out in the claims which are appended hereto and made a part hereof.
In the drawings I have shown my invention in the best form now known to me, and in the following description of my improvement I will specifically refer thereto.
In said drawings, Figure l is a vertical section of a cell or containing vessel showing my improved diaphragm. Fig. 2 shows the upper portion of the central frame hereinafter referred to. Fig. 3 is a perspective of a portion of the side frame in which the carbon electrode is supported. Fig. 4 is a similar view of the other side frame in which the negative electrode is supported. Fig. 5 is a detail on a smaller scale, which is hereinafter referred to.
My invention is simple-and will be readily understood from the following description in which the construction is set forth. The outer containing vessel or cell is shown at A, and may be of any well-known shape or construction. The brine or solution which is to be decomposed is contained within this cell, the level of the liquid therein being indicated at a. An overflow isshown at b which serves to. prevent the liquid in the positive electrode compartment of the cell from rising above the level indicated. If required a similar overflow may be provided in the negative electrode compartment, as indicated by dotted lines in Fig. 1. A frame, which I have termed the central frame is shown at c and is constructed of suitable material as lead, for example, and made to fit the interior of the cell A closely. The cross piece d at the top of the frame 0 is joined to the upright portions level of which is somewhat higher than that of the frame somewhatbelow the top thereof as shownFig. 2 so as to leavethe uprights projecting above the cross piece. A series of holes 6 which pass vertically through the cross piece at are made therein. frainecare made true so that a diaphragm or layer of material may be securely clamped thereon said layer or diaphragm being secured IOO The sides of the the passage of the current. The layer f is secured in place by clamping it betweenthe frame a and a side frame g which supports the positive or carbon electrode 71.. A series of rods are placed in the frame g crosswise thereof and adjacent the layer or sheet f. The rods 7c are preferably secured in place by being laid in aslot or recess provided ateach end of each rod in the uprightportion of the side frame g as shown Fig. 3. The rods it serve to prevent the asbestus layer f from bulging toward the carbon electrode. On the other side of the frame 0 I placeanother side frame Z shown Fig. 4E between which and the frame 0 is clamped a layer ,orsheet of parchment m or a material having the qualities of parchment and ofwhich parchment is the type. In the frame Z the negative electrode which may be a sheet of iron netting is preferably secured adjacent theparchment sheetand serves to prevent said sheet from bulging toward the negative side of the cell. The positive wireis indicated at qand the negative wire at 0*. These wires are shown as connected with the positive and negative electrode respectively. Itis unnecessary to do more than indicate the connections as the details thereof are merely matters of electri cal engineering and well known to those skilled in the art. The diaphragm proper, that is the parchment layer m is separated from the layer or sheet of asbestos f by the thickness of the frame a and this may bevaried as desired without departing from my invention. The space betweenthe layers or sheets m and f is provided with brine which is supplied as desired to .the space shown at s Fig. 1 directly above the cross piece cl of the central frame 0. This brine passes down through the holes 6 into the space below the said cross piece at and between the layers m and f. The level of the liquid in the intermediate space between said layers is maintained at a higher level than the level a of the liquid outside said space. This causes a flow of the liquid outwardly through the pervious asbestos layer from the space between the layers m f toward the positive electrode side of the cell and thus serves to prevent the chlorine or any of the liquid containing chlorine from reaching the parchment diaphragm m. As the parchment is quite durable unless attacked by the chlorine its life isin this way prolonged and its efiectiveness secured. As the layer of asbestos f is not attacked by chlorine its full efficiency is also obtained and a diaphragm of great durability and efficiency is the result. As previously stated the inter-diaphragm space between the layers m f is supplied with fresh solution and as this solution constantly flows through the pervious asbestus layer into the positive compartment of the cell, the electrolyte supply for the positive compartment is wholly orki largely furnished in this way. The eifect of the excess of pressure due to the higher ,levelofthe liquid in the inter-diaphragm space is to minimize and render of no importance the diffusion of chlorinated solution toward the parchment sheet which electrically considered is the diaphragm proper. It .willbe clear that the value of my device does not depend upon the use of either parchment orasbestusfor the sheetsm f and I do not t herefore desire to confine myself to suclr'sheets. Many substances maybe used in place of thesematerials. As an equivalent for the parchment I may mention a bich-romatized gelatine which has been rendered insoluble by exposure to the sun-light and very thick woven cloth fabric. Inplace of the .asbestus thin porousearthenware may be. used.
In case the products ofdecompositionat the negative electrode is sufficient to destroy or render it desirable to protect, the diaphragm or non-poroussheet m from their action the negative electrode may be removed somewhat from the I said diaphragm-and a pervious sheet similar to the sheet f may be placed on the negativesideof thesheet m, ina manner similar to that in which it is shown as arranged on the positive side in the drawings and the supply of the solution for the negative compartment maybe caused to take place through this pervious sheet. In other words the arrangement shown in Fig. 1 is for use in caseswhere the products of decomposition which are liberated at the negative electrode are notsuch aswill attack theparchmentsheet. In case, however these products are injurious to the parchment sheet and the parchment sheet {requires to be protected therefrom it is only necessary to duplicate the pervious sheet shown in Fig. l on the negative side of the diaphragm proper thus providing for a flow of liquid from theintermediate space into the negative compartment thus securing the diaphragm from attack on that side. Such a construction is shown in Fig. 5. The central frame a maybe made by cutting it from heavy sheets of lead. The holes 6 in the cross bar (1 of said frame not onlyserve for the admission of the solution but also for .the escape of any bubbles of gas which may be liberated in the inter-diaphragm space. The negative electrode frame Z is preferably of slate but it may be of high qualitystone ware or of glass. The rods 70 are also preferably of glass.
The device employed for clamping the frames together is not shown butany well known clamp may be employed.
The frames employed for supporting the diaphragm as also the pervious sheet or sheets may be varied as will be obvious in form and construction without departing from my invention, the important feature of which is the separation of the diaphragm proper from'the corrosive product by the interposition of a pervious sheet and fresh liquid, the latter flowing away from the diaphragm.
What I claim is- 1. An electrolytic cell having in combination with the diaphragm thereof a pervious sheet or layer interposed between said diaphragm and the electrode of the cell, and separated from said diaphragm by a space forming a chamber containing liquid under greater relative pressure than the liquid in the adjacent compartment of thecell, whereby the movement of the liquid in the cell due to the said greater pressure will be from said diaphragm and through the pervious sheet or layer, substantially as set forth.
2. In an electrolytic cell, the combination with the diaphragm of'a sheet or layer separated from said diaphragm and interposed between the same and the electrode of the cell, and suitable frames for preventing said dia phragm and said pervious sheet from bulging under the pressure of the liquid, all substantially as described, and whereby the level of the liquid in the space between the diaphragm and the pervious sheet may be maintained at a higher level than the level of the liquid in the compartment of the cell, sub- 'stanti ally as set forth,
3. The combination with the cell A provided with a suitable overflow b, of the frame 0 provided with holes e, the diaphragmmand pervious sheet f at opposite sides of the frame a and the side frames g Z, for the electrodes, placedrespectively beside the said pervious sheet and the diaphragm substantially as shown and described.
4. The combination with the frame a of the pervious layer f at one side thereof and the frame g and rods 70, at the side of the pervious layer substantially as shown and described. 5. The method of protecting the diaphragm of an electrolytic cell, which consists in first producing a diaphragm wall or layer of fluid between'the said diaphragm and the contents of the cell adjacent to the said diaphragm, then occasioning pressure upon the fluid, and keeping the latter under pressure and thereby maintaining in the said fluid lateral pressure with tendency to lateral flow away from the diaphragm, substantially as described.
In testimony whereof I affix my signature in presence of two witnesses.
ERNEST ARTHUR LE SUEUR.
Witnesses: WM. A. MACLEOD,
RoBT. WALLACE.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2846384A (en) * 1953-12-05 1958-08-05 Oronzio De Nora Impianti Bipolar electrolyser

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2846384A (en) * 1953-12-05 1958-08-05 Oronzio De Nora Impianti Bipolar electrolyser

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