US2222979A - Anode for electrolyzers with vertical diaphragms - Google Patents

Anode for electrolyzers with vertical diaphragms Download PDF

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US2222979A
US2222979A US218494A US21849438A US2222979A US 2222979 A US2222979 A US 2222979A US 218494 A US218494 A US 218494A US 21849438 A US21849438 A US 21849438A US 2222979 A US2222979 A US 2222979A
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anode
rod
frame
electrolyzers
bore
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US218494A
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Lemaire Jacques Philippe
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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
    • C25B9/60Constructional parts of cells
    • C25B9/65Means for supplying current; Electrode connections; Electric inter-cell connections
    • 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

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  • the duration of the carbon anodes whichare used in electrolyzing devices of the type with vertical diaphragms is (obviously without giving consideration to the intrinsic quality of the carbons) a function of the greater or smaller degree of perfection of the parallelism between anodes and cathodes.
  • the main feature of my invention consists in that the carbon anode is formed of a circular or prismatic cylinder which is bored axially and provided with a dummy hole which is large enough for receiving a carrying rod made of a material which is unattackable by the solution to be electrolyzed and by the products of the electrolysis.
  • This rod is immobilized in the transverse direction in its lower part; the anode is slid onto the rod and rests through the bottom of its hole on the upper part of the said rod.
  • the transverse dimensions of the hole and of the rod are such that the play between the same is small. Under these conditions the anode is supported and centered.
  • the means provided for immobilizing the lower part of the carrier rod is so located in the cell that both parts of the anode which are opposite the cathodes are equi-distant from the latter.
  • the current is fed to the anode preferably through a carbon rod which is fast, for instance by screwing therein, with the upper part of the anode.
  • the lower end of this rod may form the bottom of the anode hole.
  • Fig. 1 is a perspective elevational view with partial tearing away of a part of such a cell.
  • Fig. 2 is a cross sectional view of an electrolytic cell according to my invention
  • the cell comprises, in the usual manner, a frame I on both sides of which the'cathod'e elements -2*.are applied and 'maintained byany known :suitable'device;
  • the usual diaphragms are shown at 3 ( Figure 2),.
  • recesses 4 which are equi-distantfromzboth cathode e1emen ts'2, 3.
  • In thesezrecesses' are vertically lodged glass rods .5.
  • On each .of these rods is slid an elementary anode! provided, forthis purpose, with an axial ho1e8 having a diameter slightly larger than the diameter of. therod '5;
  • the axial bore of the elementary anodes permits a more regular impregnation of the latter, the penetration of the impregnation liquid (such as linseed-oil, for instance) taking place both from inward and from outward. Furthermore, the air which is confined in the pores of the carbons being able more easily to escape during the impregnation, there is less reason to fear that parts of the carbons could not be impregnated.
  • the impregnation liquid such as linseed-oil, for instance
  • an anode having a reduced portion of circular cross section extending through and laterally supported in the top of said frame, the majorportion of said anode being cylindrical and having an axial bore entering from the bottom of said anode and terminating above the center of gravity thereof, said frame having a recess in the bot--- King a reduced portion of circular cross section extending through and laterally supported in tom thereof, and a rod of non-attackable material slightly smaller in diameter than said bore so as to fit loosely therein, and of a length greater than the sum of the length of said bore plus the depth of said recess disposed within said bore with its lower end projecting Ithere-a from and seated in said recess to support said anode vertically and laterally.
  • anode having a-major portion of cylindrical form and having non-attackable material slightly smaller in diameter than said bore so as to fit loosely therein, and of a length greater than the sum of the length of the unthreaded portion of said bore plus the depth of said recess to project from said bore when situated therein with an end of said rod abutting said threaded conducting member, the projecting end of said rod being seated in said recess to support said anode vertically and laterally.
  • an electrolyzer having vertical diaphragms supported on a frame an anode havthetop of said frame, a gas type packing on the top of said frame and surrounding said re- 'duced portion, the major portion of said anode being cylindrical and having an axial bore entering. from the bottom of said anode and ter- Ini'nating above the center of gravity thereof, said.

Description

Nov. 26, 1940. J.-P. LEMAIRE ANODE FOR ELECTROLYZERS WITH VERTICAL DIAPHRAGMS Filed July 11, 1938 IN VENTOR. IJ4CQUE6 PHIL IPPE LEMAI lfE.
AT TO RN EYS- Patented Nov. 26, 1940 UNITED s'rAT-Es PATENT- 'd()FEICE. 2,222,979 1 Jacques Philippe Ircmaire, Lille, France July 11, 1938, SerialNo-218,494 In France July .22, .1937
Application 3 Claims.
The duration of the carbon anodes whichare used in electrolyzing devices of the type with vertical diaphragms is (obviously without giving consideration to the intrinsic quality of the carbons) a function of the greater or smaller degree of perfection of the parallelism between anodes and cathodes.
Indeed, if the said parallelism is not a perfect one, afiluxes of current take place in the carbons at the points where they are nearest to the electrodes. These local overloads cause, of course, their disintegration and their prema tured wear.
This inconvenience is avoided by the arrangements which form the subject matter of my present invention. The main feature of my invention consists in that the carbon anode is formed of a circular or prismatic cylinder which is bored axially and provided with a dummy hole which is large enough for receiving a carrying rod made of a material which is unattackable by the solution to be electrolyzed and by the products of the electrolysis. This rod is immobilized in the transverse direction in its lower part; the anode is slid onto the rod and rests through the bottom of its hole on the upper part of the said rod. The transverse dimensions of the hole and of the rod are such that the play between the same is small. Under these conditions the anode is supported and centered. The means provided for immobilizing the lower part of the carrier rod is so located in the cell that both parts of the anode which are opposite the cathodes are equi-distant from the latter.
The current is fed to the anode preferably through a carbon rod which is fast, for instance by screwing therein, with the upper part of the anode. The lower end of this rod may form the bottom of the anode hole.
Owing to this arrangement for the anode, it is easy to insure the tightness for the passage of the rod which supplies the current through the ceiling of the gas chamber, this tightness being here obtained through a mere casting of packing cement or mastic.
An embodiment of my invention is shown by way of example in the appended drawing.
In this drawing: 7
Fig. 1 is a perspective elevational view with partial tearing away of a part of such a cell.
Fig. 2 is a cross sectional view of an electrolytic cell according to my invention;
In the form of execution shown in the drawing the cell comprises, in the usual manner, a frame I on both sides of which the'cathod'e elements -2*.are applied and 'maintained byany known :suitable'device; The usual diaphragms are shown at 3 (Figure 2),. In the lower-beam of the frame I are provided recesses 4 which are equi-distantfromzboth cathode e1emen ts'2, 3. In thesezrecesses' are vertically lodged glass rods .5. On each .of these rods is slid an elementary anode! provided, forthis purpose, with an axial ho1e8 having a diameter slightly larger than the diameter of. therod '5;
' of .the hole 8 is closed by a carbon rod 9 located in the upper part of the elementary anode I. By the lower par-t of this rod 9, the anode is thus suspended on the upper end of the rod 5. The carbon rod 9 passes through the ceiling ll] of the gas chamber formed by the upper partsubdivided in two portionsof theframe I. The packing joint between the rod '9 and the. ceiling ID is obtained by pouring onto the ceiling In, which is located slightly below the upper part of the frame I, a grout of tarry cement such as those which are usually'e'mployed in sealing of electrolytic-cells.
From the above information, it resultslclearly that the position of the elementary anodes with respect to the cathode elements is insured in a correct manner as to the parallelism between: anode and cathode, for the elementary anodes cannot undergo any lateral sliding movement and they rest by their own weight on a rigid carrier at a point which is subject neither to wear nor to deterioration and which is located above their center of gravity. These elementary anodes will always keep in the electrolyzer, as long as there remains some thickness of carbon about the carrier rod 5, their-rigid vertical position and their perfect alignment in the middle plane of the cathodes. Their distances with respect to the latter will thus always be identical and regular. On the other hand it is easy, by rotating the anodes about their axis, to modify their orientation in order to bring new parts of elementary anodes opposite the cathodes when the said anodes have undergone a wear sufficient for causing an undesirable increase of the voltage between anode and cathode.
Finally, the axial bore of the elementary anodes permits a more regular impregnation of the latter, the penetration of the impregnation liquid (such as linseed-oil, for instance) taking place both from inward and from outward. Furthermore, the air which is confined in the pores of the carbons being able more easily to escape during the impregnation, there is less reason to fear that parts of the carbons could not be impregnated.
What I claim is:
1. In an electrolyzer having vertical diaphragms supported on a frame, an anode having a reduced portion of circular cross section extending through and laterally supported in the top of said frame, the majorportion of said anode being cylindrical and having an axial bore entering from the bottom of said anode and terminating above the center of gravity thereof, said frame having a recess in the bot--- King a reduced portion of circular cross section extending through and laterally supported in tom thereof, and a rod of non-attackable material slightly smaller in diameter than said bore so as to fit loosely therein, and of a length greater than the sum of the length of said bore plus the depth of said recess disposed within said bore with its lower end projecting Ithere-a from and seated in said recess to support said anode vertically and laterally. s 2. In an electrolyzer having Vertical diaphragms supported on a frame, an anode having a-major portion of cylindrical form and having non-attackable material slightly smaller in diameter than said bore so as to fit loosely therein, and of a length greater than the sum of the length of the unthreaded portion of said bore plus the depth of said recess to project from said bore when situated therein with an end of said rod abutting said threaded conducting member, the projecting end of said rod being seated in said recess to support said anode vertically and laterally.
3. In an electrolyzer having vertical diaphragms supported on a frame an anode havthetop of said frame, a gas type packing on the top of said frame and surrounding said re- 'duced portion, the major portion of said anode being cylindrical and having an axial bore entering. from the bottom of said anode and ter- Ini'nating above the center of gravity thereof, said. frame having a recess in the bottom thereof; and a rod of non-attackab-le material slightly smaller in diameterthan said boreso as to fit loosely therein, and of a length greater than the sumcf the length of said bore plus the depth of said recess disposed within said bore with its lower end projecting therefrom and seated in said recess to support said anode vertically and laterally.
JACQUES PHILIPPE LEMAIRE.
US218494A 1937-07-22 1938-07-11 Anode for electrolyzers with vertical diaphragms Expired - Lifetime US2222979A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3133872A (en) * 1959-03-10 1964-05-19 Chemionics Engineering Lab Inc Anode for electrochemical applications
US3461057A (en) * 1964-08-20 1969-08-12 Georgy Mikirtychevich Kamarjan Diaphragm electrolyzer for production of chlorine,hydrogen and alkalies
US3985636A (en) * 1975-09-26 1976-10-12 Aqua-Chem, Inc. Electrodialysis apparatus electrode system
US6129822A (en) * 1996-09-09 2000-10-10 Ferdman; Alla Insoluble titanium-lead anode for sulfate electrolytes

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3133872A (en) * 1959-03-10 1964-05-19 Chemionics Engineering Lab Inc Anode for electrochemical applications
US3461057A (en) * 1964-08-20 1969-08-12 Georgy Mikirtychevich Kamarjan Diaphragm electrolyzer for production of chlorine,hydrogen and alkalies
US3985636A (en) * 1975-09-26 1976-10-12 Aqua-Chem, Inc. Electrodialysis apparatus electrode system
US6129822A (en) * 1996-09-09 2000-10-10 Ferdman; Alla Insoluble titanium-lead anode for sulfate electrolytes

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