US3884781A - Processes for the electrolysis of alkali halides employing dismantleable bipolar electrodes - Google Patents
Processes for the electrolysis of alkali halides employing dismantleable bipolar electrodes Download PDFInfo
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- US3884781A US3884781A US431024A US43102474A US3884781A US 3884781 A US3884781 A US 3884781A US 431024 A US431024 A US 431024A US 43102474 A US43102474 A US 43102474A US 3884781 A US3884781 A US 3884781A
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- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 15
- 150000004820 halides Chemical class 0.000 title claims abstract description 11
- 238000000034 method Methods 0.000 title claims abstract description 11
- 239000003513 alkali Substances 0.000 title abstract description 7
- 229910052751 metal Inorganic materials 0.000 claims abstract description 29
- 239000002184 metal Substances 0.000 claims abstract description 29
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 abstract description 15
- 229910052719 titanium Inorganic materials 0.000 abstract description 15
- 239000010936 titanium Substances 0.000 abstract description 15
- 229910001209 Low-carbon steel Inorganic materials 0.000 abstract description 10
- 229910045601 alloy Inorganic materials 0.000 abstract description 10
- 239000000956 alloy Substances 0.000 abstract description 10
- 238000000926 separation method Methods 0.000 abstract description 4
- 150000002739 metals Chemical class 0.000 description 11
- 238000005192 partition Methods 0.000 description 9
- 125000006850 spacer group Chemical group 0.000 description 7
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 4
- 238000007789 sealing Methods 0.000 description 4
- 239000000460 chlorine Substances 0.000 description 3
- 238000010276 construction Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 239000004020 conductor Substances 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- IUYOGGFTLHZHEG-UHFFFAOYSA-N copper titanium Chemical compound [Ti].[Cu] IUYOGGFTLHZHEG-UHFFFAOYSA-N 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000014509 gene expression Effects 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229910052758 niobium Inorganic materials 0.000 description 1
- 239000010955 niobium Substances 0.000 description 1
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 150000003057 platinum Chemical class 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 229910052703 rhodium Inorganic materials 0.000 description 1
- 239000010948 rhodium Substances 0.000 description 1
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
- 239000011265 semifinished product Substances 0.000 description 1
- 229910052715 tantalum Inorganic materials 0.000 description 1
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/60—Constructional parts of cells
- C25B9/65—Means for supplying current; Electrode connections; Electric inter-cell connections
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/02—Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form
- C25B11/03—Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form perforated or foraminous
Definitions
- Said electrodes are characterized by the separation in space of said active portions, at least one of which is apertured or foraminous, and by the electrical connection between said portions, which is achieved by means of two series of parts, each of said series being mechanically and electrically secured to one of said portions, the corresponding parts of each series being of shapes such that once connected in order to form pairs of parts, said pairs have a sealed cavity for housing a device or means for establishing electrical contact between the two parts of each pair.
- Electrodes are particularly suited for being mounted in cells of the filter-press type, for the electrolysis of brines.
- This invention concerns processes for electrolysis of alkali halides employing dismantleable bipolar electrodes of which the anodically and cathodically active portions are separated in space.
- bipolar electrodes When electrically connected in series they permit high power to be used for a given floor area and simplify the supplying of electricity.
- This type of electrode has long been known.
- the active portions thereof can be planar or can be of other shapes, for example corrugated, in order to increase their electrolysis surface area.
- metals of suitable anodic behaviour such as the filmforming metals, including titanium, zirconium, tantalum, niobium and tungsten, and also alloys of such metals, when covered with thin layers of precious metals, has also long been known.
- the filmforming metals including titanium, zirconium, tantalum, niobium and tungsten, and also alloys of such metals, when covered with thin layers of precious metals.
- the electrolytically active conducting layers can be oxides of such metals or mixtures of various oxides.
- the electrolysis industry is at present proposing a certain number of mixed semi-finished products such as bars formed by metals which are good conductors, such as copper or aluminum, sheathed with metals such as titanium or alloys of similar anodic properties, the use of which makes it possible considerably to reduce the voltage drops in various component portions of metal anodes.
- At least one of the portions is apertured, and connected electrically and mechanically by means of mixed parts of common metal, which can be used cathodically, such as mild steel, plated with titanium or other film-forming metal or alloy of similar anodic properties.
- common metal which can be used cathodically, such as mild steel, plated with titanium or other film-forming metal or alloy of similar anodic properties.
- partition separating the electrolytically active portions in order to prevent attack and untimely current leakage.
- bipolar electrodes with non-planar electrolytically active portions have been proposed, wherein the latter are mounted on respective sides of a partition by means of screwthreaded parts, for example, which makes them dismantleable.
- These solutions which are satisfactory from the mechanical point of view, are less so from the electrical point of view, owing to the dubious passage of the current which, according to the quality of the contacts made. passes to a greater or lesser extent between conducting surfaces which are tightened together, and by way of the body of the screw-threaded parts of the assembly. This means that the resistances of such contacts are always relatively high, are not always the same for the different points at which contact is made in the same electrode, and moreover develop differently in use.
- FIG. 1 is a section of a portion of a bipolar electrode of the invention.
- FIG. 2 is a complete electrode according to the invention.
- FIG. 3 is a cross-section of the electrode taken along the line A-'A of FIG. 2.
- FIG. 4 shows a form of a portionof another embodi ment of the invention, in which the coupled anodic and cathodic portions are corrugated to increase surface area.
- the present applicants have been able to overcome these very serious disadvantages of the prior art dismantleable bipolar electrodes, by specially designed electrical connections between the anodically and cathodically active portions of the electrode.
- the proposed novel type of bipolar electrode concerns electrodes in which the anodically active portion comprises titanium or a similar film-forming metal or alloy, covered with a thin unattackable, corrosion-resistant conducting layer, and the cathodically active portion comprises a suitable metal, such as mild steel or nickel, which anodically and cathodically active portions are separated in space and can be of any shape, although in most cases planar or corrugated shapes are preferred, at least one of said portions being apertured of a foraminous nature.
- the electrical connection between said portions is produced by welding on to each one, directly or by the intermediary of spacer means, which, on the anodic side, can comprise metals which are good electrical conductors, sheathed with titanium or similar film-forming metals or alloys, series of parts, said parts of each electrolytically active portion corresponding to respective parts of the other portion.
- spacer means which, on the anodic side, can comprise metals which are good electrical conductors, sheathed with titanium or similar film-forming metals or alloys, series of parts, said parts of each electrolytically active portion corresponding to respective parts of the other portion.
- Such a construction makes the contacts independent of the tightening of the parts, such tightening serving only to ensure that the assembly is rigidly made, and is sealed.
- various solutions can be found for making the internal contacts within the cavity defined in each pair of parts.
- Such contacts can be effected for example by means of a liquefied alloy or metal or by one or more springs which bear against each of the two parts to be brought into electrical contact.
- Such springs can be. for example, formed of a multiplicity of resilient plates or can be in the shape of coil springs, possibly provided with graphite and pieces connected by conducting braids.
- the internal surfaces of the cavities within which the contacts are made can be treated in any known manner for improving the contact, whether by scouring, increasing the surface areas, various metal deposits or any other method.
- electrolytically active portions anodes and cathodes
- a partition between the portions, in order to prevent the electrolytically active portions being attacked, or even to prevent the anolyte mixing with the catholyte, and the current leakage which would result.
- a partition can comprise materials which are not liable to attack either by the anolyte or by the catholyte, such as some plastics materials, or it can comprise a metal wall which can have two faces of different nature, but which are not liable to attack by the electrolyte with which each of the faces is in contact.
- the partition wall When the partition wall is metal, it can be welded to the parts forming a pair, which parts are welded to the electrolytically active portions.
- the partition When the partition is of a non-metallic material, it can be tightened on to the parts of the same electrolytically active portion or between the parts forming pairs. In these various cases, scaling is ensured by means of seal means which can be the same as those intended to seal the two parts forming each pair relative to each other.
- bipolar electrodes can be produced and are part of the present invention. Some embodiments are described hereinafter by way of example and illustration.
- FIG. 1 shows a detail of one of the pairs of parts, and a part of the anodic and cathodic portions of the bipolar electrode which are welded thereto.
- Reference 1 denotes one of the parts of the pair, which comprises titanium
- reference 2 denotes the second part which comprises mild steel.
- the anodic portion of the bipolar electrode comprises an expanded apertured or foraminous titanium sheet 6 welded to the part 1 by means of a jointly drawn memher 7 of copper and titanium which extends over the entire height of the electode and acts as a spacer member.
- the cathode 8 which comprises a mild steel wire open grid is welded to the other part 2 of the pair, through the intermediary of a mild steel plate 9 which also extends over the entire height of the electrode and which acts as a spacer member. Separation of the ano lyte' and the catholyte is ensured by a polyester partition 10 which is gripped between the two parts I and 2, sealing being effected by seal means ll.
- FIG. 2 shows a complete electrode
- FIG. 3 shows a cross-section of the electrode, through two pairs of parts for making an electrical connection between the anodic and cathodic portions.
- Reference 12 denotes a polyester frame which is provided with a veil means which is the partition 10 for separating the anodic portion 6 and the cathodic portion 8 of each of the six electrode elements 13 forming the complete electrode.
- the pairs of parts 1 and 2 are denoted by reference 14.
- Reference 7 denotes the copper-titanium members which are drawn jointly, acting as spacer members between the anodic portions 6 and the parts 1
- reference 9 denotes the mild steel plates acting as spacer members between the cathodic portions 8 and the parts 2. Details of the sealing gaskets and the clamping screws are not shown in FIGS. 2 and 3.
- EXAMPLE 2 This example relates to FIG. 4 of the accompanying drawings, and relates to the use of a coupling device according to the present invention in a bipolar electrode in which the anodic and cathodic portions are corrugated in order to increase the contact surface area.
- Reference l4 diagrammatically denotes a pair of parts identical to those described in the preceding example, the sealing means and the tightening means not being shown in this Figure.
- the partition is diagrammatically indicated by reference 10.
- the anodic portion 15 which comprises an expanded apertured and corrugated sheet of titanium covered with platinum is welded to the corresponding part of the pair by means of a copper-titanium jointly drawn member acting as a spacer member 16;
- the corrugated cathodic portion 17 which comprises a mild steel open grid is welded to the corresponding part of the pair 14 by means of a mild steel plate l8 acting as a spacer member.
- components of titanium may be replaced by components of similar construction comprised of other film-forming metals.
- each of said series being mechanically and electrically fixed with respect to one of said portions, the corresponding parts of each series being of shapes such that once connected in order to form pairs of parts, said pairs define a sealed cavity for housing a device or means for establishing an electrical Contact between the parts of each pair which process comprises feeding an alkali halide to said electrolytic cell employing said dismantleable bipolar electrodes and applying an electrical current to the said dismantleable bipolar electrodes to electrolyze the alkali halide.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
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- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Electrolytic Production Of Metals (AREA)
Abstract
Processes for the electrolysis of alkali halides employing dismantleable bipolar electrodes are provided of which the anodically active portion comprises titanium or other filmforming metal or alloy of similar anodic properties covered with a conducting layer, and of which the cathodically active portion comprises a common metal such as mild steel. Said electrodes are characterized by the separation in space of said active portions, at least one of which is apertured or foraminous, and by the electrical connection between said portions, which is achieved by means of two series of parts, each of said series being mechanically and electrically secured to one of said portions, the corresponding parts of each series being of shapes such that once connected in order to form pairs of parts, said pairs have a sealed cavity for housing a device or means for establishing electrical contact between the two parts of each pair. These electrodes are particularly suited for being mounted in cells of the filter-press type, for the electrolysis of brines.
Description
United States Patent Bouy et a].
[111 3,884,781 [451 May 20, 1975 PROCESSES FOR THE ELECTROLYSIS OF [75] Inventors: Pierre Bouy, Ehghien-Les-Bains;
Guillaume Malzac, Martigues, both of France [73] Assignee: Rhone-Progil, Paris, France [22] Filed: Jan. 7, 1974 [21] Appl. No.: 431,024
Related US. Application Data [62] Division of Ser. No. 314,783, Dec. 13, 1972, Pat. No.
[30] Foreign Application Priority Data Dec. 22, 1971 France "71.46072 [52] US. Cl. 204/98; 204/95; 204/128', 204/129; 204/279 [51] Int. Cl C01d 1/06 [58] Field of Search 204/95, 98, 128, 256, 268, 204/279, 129
[56] References Cited FOREIGN PATENTS OR APPLICATIONS 669,590 8/1963 Canada 204/279 Primary Examiner-John H. Mack Assistant Examiner-W. 1. Solomon [57] ABSTRACT Processes for the electrolysis of alkali halides employing dismantle-able bipolar electrodes are provided of which the anodically active portion comprises titanium or other film-forming metal or alloy of similar anodic properties covered with a conducting layer, and of which the cathodically active portion comprises a common metal such as mild steel. Said electrodes are characterized by the separation in space of said active portions, at least one of which is apertured or foraminous, and by the electrical connection between said portions, which is achieved by means of two series of parts, each of said series being mechanically and electrically secured to one of said portions, the corresponding parts of each series being of shapes such that once connected in order to form pairs of parts, said pairs have a sealed cavity for housing a device or means for establishing electrical contact between the two parts of each pair.
These electrodes are particularly suited for being mounted in cells of the filter-press type, for the electrolysis of brines.
1 Claim, 4 Drawing Figures 555mmairwa s 3384781 SHEET 10F 3 Pics. 1
PROCESSES FOR THE ELECTROLYSIS OF ALKALI HALIDES EMPLOYING DISMANTLEABLE BIPOLAR ELECTRODES This application is a division of our copending application, Ser. No. 314,783, filed Dec. 13, 1972 now US. Pat. No. 3,824,173.
BACKGROUND OF THE INVENTION This invention concerns processes for electrolysis of alkali halides employing dismantleable bipolar electrodes of which the anodically and cathodically active portions are separated in space.
The advantages of bipolar electrodes are known. When electrically connected in series they permit high power to be used for a given floor area and simplify the supplying of electricity. This type of electrode has long been known. The active portions thereof can be planar or can be of other shapes, for example corrugated, in order to increase their electrolysis surface area.
However, the early types proposed could use only a small number of materials available at that time, which, because of their cost or their deficiency in respect of mechanical and electrical properties, did not permit satisfactory solutions to be achieved, at least as regards some uses such as the electrolysis of alkaline chloride solutions for producing therefrom chlorine and alkaline lyes.
The possibility of using for electrolysis purposes metals of suitable anodic behaviour, such as the filmforming metals, including titanium, zirconium, tantalum, niobium and tungsten, and also alloys of such metals, when covered with thin layers of precious metals, has also long been known. However, it is only since titanium has become the most commonly available metal of this group, owing to its use in large quantities for other purposes, that numerous electrolytic devices using titanium have been proposed. Besides metals of the platinum series, including platinum per se. and rhodium. the electrolytically active conducting layers can be oxides of such metals or mixtures of various oxides. Moreover, the electrolysis industry is at present proposing a certain number of mixed semi-finished products such as bars formed by metals which are good conductors, such as copper or aluminum, sheathed with metals such as titanium or alloys of similar anodic properties, the use of which makes it possible considerably to reduce the voltage drops in various component portions of metal anodes.
However, the use in electrolysis of titanium or other film-forming metals or alloys of similar anodic behavior, permits a very substantial increase in the current densities, so that solutions must be found for the problems of discharging the gases produced, such solutions comprising for example the use of apertured electrodes. In the case of bipolar electrodes, this leads to separation of the anodically and cathodically active portions. As disclosed in concurrently filed application, Ser. No. 314,728, entitled Bipolar Electrodes, corresponding to an earlier French patent application of one of applicants with Daniel Collard, filed Dec. 21, 197] under the No. 7l4586l, the applicants propose electrodes in which the electrolytically-active portions, which can be planar or of any other shape, for example, corrugated. At least one of the portions is apertured, and connected electrically and mechanically by means of mixed parts of common metal, which can be used cathodically, such as mild steel, plated with titanium or other film-forming metal or alloy of similar anodic properties. There is a partition separating the electrolytically active portions in order to prevent attack and untimely current leakage.
Various other embodiments of bipolar electrodes with non-planar electrolytically active portions have been proposed, wherein the latter are mounted on respective sides of a partition by means of screwthreaded parts, for example, which makes them dismantleable. These solutions, which are satisfactory from the mechanical point of view, are less so from the electrical point of view, owing to the dubious passage of the current which, according to the quality of the contacts made. passes to a greater or lesser extent between conducting surfaces which are tightened together, and by way of the body of the screw-threaded parts of the assembly. This means that the resistances of such contacts are always relatively high, are not always the same for the different points at which contact is made in the same electrode, and moreover develop differently in use.
It is an object of the present invention to provide dismantleable bipolar electrodes which are free from the foregoing defects.
It is another object of the present invention to provide bipolar electrodes which are readily dismantled.
objects of the invention will be apparent to those skilled in the art from the present description, taken in conjunction with the appended drawings, in which:
FIG. 1 is a section of a portion of a bipolar electrode of the invention.
FIG. 2 is a complete electrode according to the invention.
FIG. 3 is a cross-section of the electrode taken along the line A-'A of FIG. 2.
FIG. 4 shows a form of a portionof another embodi ment of the invention, in which the coupled anodic and cathodic portions are corrugated to increase surface area.-
GENERAL DESCRIPTIONOF THE INVENTION The present applicants have been able to overcome these very serious disadvantages of the prior art dismantleable bipolar electrodes, by specially designed electrical connections between the anodically and cathodically active portions of the electrode. The proposed novel type of bipolar electrode concerns electrodes in which the anodically active portion comprises titanium or a similar film-forming metal or alloy, covered with a thin unattackable, corrosion-resistant conducting layer, and the cathodically active portion comprises a suitable metal, such as mild steel or nickel, which anodically and cathodically active portions are separated in space and can be of any shape, although in most cases planar or corrugated shapes are preferred, at least one of said portions being apertured of a foraminous nature. The electrical connection between said portions is produced by welding on to each one, directly or by the intermediary of spacer means, which, on the anodic side, can comprise metals which are good electrical conductors, sheathed with titanium or similar film-forming metals or alloys, series of parts, said parts of each electrolytically active portion corresponding to respective parts of the other portion. Each pair of parts thus formed by bringing said parts together and tightening them to each other, defines a cavity for receiving a device or means for establishing an electri- 3 cal contact between the two parts of the pair in question.
The attraction of such a construction is that it makes the contacts independent of the tightening of the parts, such tightening serving only to ensure that the assembly is rigidly made, and is sealed. In practice, various solutions can be found for making the internal contacts within the cavity defined in each pair of parts. Such contacts can be effected for example by means of a liquefied alloy or metal or by one or more springs which bear against each of the two parts to be brought into electrical contact. Such springs can be. for example, formed of a multiplicity of resilient plates or can be in the shape of coil springs, possibly provided with graphite and pieces connected by conducting braids.
Obviously, the internal surfaces of the cavities within which the contacts are made can be treated in any known manner for improving the contact, whether by scouring, increasing the surface areas, various metal deposits or any other method.
It is obvious that such constructions require that the assembly of the pairs of parts should be sealed, which can conveniently be effected by means of one or more seal means made of elastomers which are resistant to the electrolytic medium in question.
It is apparent that using electrolytically active portions (anodes and cathodes), of which at least one is apertured or ofa foraminous nature, requires the provision ofa partition between the portions, in order to prevent the electrolytically active portions being attacked, or even to prevent the anolyte mixing with the catholyte, and the current leakage which would result. Such a partition can comprise materials which are not liable to attack either by the anolyte or by the catholyte, such as some plastics materials, or it can comprise a metal wall which can have two faces of different nature, but which are not liable to attack by the electrolyte with which each of the faces is in contact. When the partition wall is metal, it can be welded to the parts forming a pair, which parts are welded to the electrolytically active portions. When the partition is of a non-metallic material, it can be tightened on to the parts of the same electrolytically active portion or between the parts forming pairs. In these various cases, scaling is ensured by means of seal means which can be the same as those intended to seal the two parts forming each pair relative to each other.
SPECIFIC DESCRIPTION OF THE INVENTION Many alternative embodiments of bipolar electrodes can be produced and are part of the present invention. Some embodiments are described hereinafter by way of example and illustration.
In order to disclose more clearly the nature of the present invention, the following examples illustrating the invention are given. It should be understood, however, that this is done solely by way of example and is intended neither to delineate the scope of the invention nor limit the ambit of the appended claims.
EXAMPLE I This example describes the embodiment of FIGS. 1, 2 and 3 of the accompanying drawings. FIG. 1 shows a detail of one of the pairs of parts, and a part of the anodic and cathodic portions of the bipolar electrode which are welded thereto. Reference 1 denotes one of the parts of the pair, which comprises titanium, and reference 2 denotes the second part which comprises mild steel. These two parts are tightened together by means of a screw 3, with the interposition of a sealing gasket 4. The electrical contact between the two parts is effected by means of the ring 5 carrying resilient plate members, each of which bears simultaneously against the internal surfaces of the two parts 1 and 2. The anodic portion of the bipolar electrode comprises an expanded apertured or foraminous titanium sheet 6 welded to the part 1 by means of a jointly drawn memher 7 of copper and titanium which extends over the entire height of the electode and acts as a spacer member. The cathode 8 which comprises a mild steel wire open grid is welded to the other part 2 of the pair, through the intermediary of a mild steel plate 9 which also extends over the entire height of the electrode and which acts as a spacer member. Separation of the ano lyte' and the catholyte is ensured by a polyester partition 10 which is gripped between the two parts I and 2, sealing being effected by seal means ll.
FIG. 2 shows a complete electrode, and FIG. 3 shows a cross-section of the electrode, through two pairs of parts for making an electrical connection between the anodic and cathodic portions. Reference 12 denotes a polyester frame which is provided with a veil means which is the partition 10 for separating the anodic portion 6 and the cathodic portion 8 of each of the six electrode elements 13 forming the complete electrode. The pairs of parts 1 and 2 are denoted by reference 14. Reference 7 denotes the copper-titanium members which are drawn jointly, acting as spacer members between the anodic portions 6 and the parts 1, while reference 9 denotes the mild steel plates acting as spacer members between the cathodic portions 8 and the parts 2. Details of the sealing gaskets and the clamping screws are not shown in FIGS. 2 and 3.
EXAMPLE 2 This example relates to FIG. 4 of the accompanying drawings, and relates to the use of a coupling device according to the present invention in a bipolar electrode in which the anodic and cathodic portions are corrugated in order to increase the contact surface area. Reference l4 diagrammatically denotes a pair of parts identical to those described in the preceding example, the sealing means and the tightening means not being shown in this Figure. The partition is diagrammatically indicated by reference 10.
The anodic portion 15 which comprises an expanded apertured and corrugated sheet of titanium covered with platinum is welded to the corresponding part of the pair by means of a copper-titanium jointly drawn member acting as a spacer member 16; the corrugated cathodic portion 17 which comprises a mild steel open grid is welded to the corresponding part of the pair 14 by means of a mild steel plate l8 acting as a spacer member.
By the correspondence of the projecting parts of one electrode and the recessed parts of the electrode which follows it immediately in a cell using a series thereof, such an arrangement provides for a very substantial increase in the electrolytic surface area.
As will be apparent to those skilled in the art, components of titanium, may be replaced by components of similar construction comprised of other film-forming metals.
The terms and expressions which have been employed are used as terms of description and not of limitation, and there is no intention in the use of such terms and expressions of excluding any equivalents of the features shown and described or portions thereof. but it is recognized that various modifications are possible within the scope of the invention claimed.
What is claimed is:
l. Processes for the electrolysis of alkali halides in an electrolytic cell employing dismantleable bipolar electrodes in which the anodically active portion comprises a film-forming metal or alloy thereof. covered with a corrosion-resistant. electrical-conducting layer. and in which the cathodically active portion comprises a metal which can be used cathodically. characterized in that said active portions are separated in space, at least one of said active portions being apertured, an electrical contact between portions being produced by means of two series of parts. each of said series being mechanically and electrically fixed with respect to one of said portions, the corresponding parts of each series being of shapes such that once connected in order to form pairs of parts, said pairs define a sealed cavity for housing a device or means for establishing an electrical Contact between the parts of each pair which process comprises feeding an alkali halide to said electrolytic cell employing said dismantleable bipolar electrodes and applying an electrical current to the said dismantleable bipolar electrodes to electrolyze the alkali halide. l
Claims (1)
1. PROCESSES FOR THE ELECTROLYSIS OF ALKALI HALIDES IN AN ELECTROLYTIC CELL EMPLOYING DISMANTLEABLE BIPOLAR ELECTRODES IN WHICH THE ANODICALLY ACTIVE PORTION COMPRISES A FILM-FORMING METAL OR ALLOY THEREOF, COVERED WITH A CORROSION-RESISTANT, ELECTRICAL-CONDUCTING LAYER, AND IN WHICH THE CATHODICALLY ACTIVE PORTION COMPRISES A METAL WHICH CAN BE USED CATHODICALLY, CHARACTERIZED IN THAT SAID ACTIVE PORTIONS ARE SEPARATED IN SPACE, AT LEAST ONE OF SAID ACTIVE PORTIONS BEING APERTURES AN ELECTRICAL CONTACT BETWEEN PORTIONS BEING PRODUCED BY MEANS OF TWO SERIES OF PARTS, EACH OF SAID SERIES BEING MECHANICALLY AND ELECTRICALLY FIXED WITH RESPECT TO ONE OF SAID PORTIONS, THE CORRESPONDING PARTS OF EACH SERIES BEING OF SHAPES SUCH THAT ONCE CONNECTED IN ORDER TO FORM PAIRS OF PARTS, SAID PAIRS DEFINE A SEALED CAVITY FOR HOUSING A DEVICE OR MEANS FOR ESTABLISHING AN ELECTRICAL CONTACT BETWEEN THE PARTS OF EACH PAIR, WHICH PROCESS COMPRISES FEEDING AN ALKALI HALIDE TO SAID ELECTROLYTIC CELL EMPLOYING SAID DISMANTLEABLE BIPOLAR ELECTRODES AND APPLYING AN ELECTRICAL CURRENT TO THE SAID DISMANTLEABLE BIPOLAR ELECTRODES TO ELECTROLYZE THE ALKALI HALIDE.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US431024A US3884781A (en) | 1971-12-22 | 1974-01-07 | Processes for the electrolysis of alkali halides employing dismantleable bipolar electrodes |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR7146072A FR2164487B1 (en) | 1971-12-22 | 1971-12-22 | |
| US00314783A US3824173A (en) | 1971-12-22 | 1972-12-13 | Dismantleable bipolar electrodes including electrical contact means between the electrode portions |
| US431024A US3884781A (en) | 1971-12-22 | 1974-01-07 | Processes for the electrolysis of alkali halides employing dismantleable bipolar electrodes |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3884781A true US3884781A (en) | 1975-05-20 |
Family
ID=27249734
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US431024A Expired - Lifetime US3884781A (en) | 1971-12-22 | 1974-01-07 | Processes for the electrolysis of alkali halides employing dismantleable bipolar electrodes |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US3884781A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4115236A (en) * | 1977-12-01 | 1978-09-19 | Allied Chemical Corporation | Cell connector for bipolar electrolyzer |
| US4137145A (en) * | 1978-01-03 | 1979-01-30 | Hooker Chemicals & Plastics Corp. | Separating web for electrolytic apparatuses |
| US4137144A (en) * | 1976-03-19 | 1979-01-30 | Hooker Chemicals & Plastics Corp. | Hollow bipolar electrolytic cell anode-cathode connecting device |
| US4139448A (en) * | 1978-01-03 | 1979-02-13 | Hooker Chemicals & Plastics Corp. | Separating web - electrolytic compartment frames assembly for electrolytic apparatuses |
| WO1981000864A1 (en) * | 1979-10-01 | 1981-04-02 | Krebskosmo Chem Tech Gmbh | Composite bipolar electrode for electrolysis of alkaline metal chlorides and other electrolysis methods |
| US4560452A (en) * | 1983-03-07 | 1985-12-24 | The Dow Chemical Company | Unitary central cell element for depolarized, filter press electrolysis cells and process using said element |
| US4568434A (en) * | 1983-03-07 | 1986-02-04 | The Dow Chemical Company | Unitary central cell element for filter press electrolysis cell structure employing a zero gap configuration and process utilizing said cell |
| US4604171A (en) * | 1984-12-17 | 1986-08-05 | The Dow Chemical Company | Unitary central cell element for filter press, solid polymer electrolyte electrolysis cell structure and process using said structure |
| US5013414A (en) * | 1989-04-19 | 1991-05-07 | The Dow Chemical Company | Electrode structure for an electrolytic cell and electrolytic process used therein |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA669590A (en) * | 1963-08-27 | M. Brown Howard | Tamped connections |
-
1974
- 1974-01-07 US US431024A patent/US3884781A/en not_active Expired - Lifetime
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA669590A (en) * | 1963-08-27 | M. Brown Howard | Tamped connections |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4137144A (en) * | 1976-03-19 | 1979-01-30 | Hooker Chemicals & Plastics Corp. | Hollow bipolar electrolytic cell anode-cathode connecting device |
| US4115236A (en) * | 1977-12-01 | 1978-09-19 | Allied Chemical Corporation | Cell connector for bipolar electrolyzer |
| EP0002268A1 (en) * | 1977-12-01 | 1979-06-13 | Allied Corporation | Cell connector for bipolar electrolyzer |
| US4137145A (en) * | 1978-01-03 | 1979-01-30 | Hooker Chemicals & Plastics Corp. | Separating web for electrolytic apparatuses |
| US4139448A (en) * | 1978-01-03 | 1979-02-13 | Hooker Chemicals & Plastics Corp. | Separating web - electrolytic compartment frames assembly for electrolytic apparatuses |
| WO1981000864A1 (en) * | 1979-10-01 | 1981-04-02 | Krebskosmo Chem Tech Gmbh | Composite bipolar electrode for electrolysis of alkaline metal chlorides and other electrolysis methods |
| US4560452A (en) * | 1983-03-07 | 1985-12-24 | The Dow Chemical Company | Unitary central cell element for depolarized, filter press electrolysis cells and process using said element |
| US4568434A (en) * | 1983-03-07 | 1986-02-04 | The Dow Chemical Company | Unitary central cell element for filter press electrolysis cell structure employing a zero gap configuration and process utilizing said cell |
| US4604171A (en) * | 1984-12-17 | 1986-08-05 | The Dow Chemical Company | Unitary central cell element for filter press, solid polymer electrolyte electrolysis cell structure and process using said structure |
| US5013414A (en) * | 1989-04-19 | 1991-05-07 | The Dow Chemical Company | Electrode structure for an electrolytic cell and electrolytic process used therein |
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