Classifications

• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M10/00—Secondary cells; Manufacture thereof
  • H01M10/36—Accumulators not provided for in groups H01M10/05-H01M10/34
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/18—Regenerative fuel cells, e.g. redox flow batteries or secondary fuel cells
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
  • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
  • Y02E60/10—Energy storage using batteries
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
  • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
  • Y02E60/30—Hydrogen technology
  • Y02E60/50—Fuel cells

Definitions

• the present invention relates â ⁇ ⁇ ⁇ p ⁇ l s " l ⁇ x ⁇ " ⁇ e ⁇ " s " of electric accumulators and electrochemical generators supplying electric energy by cold combustion of an element or an oxidizable compound .
• Electrodes of these types use electrodes where the voltage and the electric current developed by the electrochemical oxidation reactions are delivered.
• accumulators or generators the oxidation of metals such as Lead, Cadmium, Zinc, Iron, Lithium, etc. or of fuels such as Hydrogen or d takes place.
• other hydrogenated or hydrocarbon compounds such as hyazine, ethanol, other alcohols or hydrocarbons, etc.
• the metals or the fuels used may require a significant expenditure of energy to be previously synthesized chemically, isolated, extracted or refined.
• the electrochemical combustion reaction in a conventional fuel cell is generally carried out under favorable conditions only by means of the use of an oxidation catalyst, often rare or expensive, such as platinum foam.
• the number of charge and discharge cycles applicable to the cells is generally limited, since the electrolytic regeneration of the electrodes, carried out at each recharging operation, may not be carried out uniformly, which affects the durability of the element.
• the regeneration operation of the accumulator or generator can only be carried out by recharging the corresponding elements electrically or by replacing altered substances or compounds.
• the object of the present invention is to constitute a battery, an accumulator or an electrochemical generator using neither a metal or a metallic compound nor a hydrocarbon or a hydrocarbon compound, but a salt existing in most cases in the state natural in unlimited quantities or that can be produced or chemically isolated without significant energy expenditure, the corresponding oxidation reaction can also be ensured without the addition of a catalyst and the electrical recharging can be carried out electrically, chemically , photonically or thermally.
• These devices according to the in-. ventioii are based on the following principles:
• the compounds used as "fuels” are chlorides and more generally halides, of alkali metals such as Sodium, Potassium or Lithium or of metals such as Ti ⁇ tane, Iron, Lead, etc.
• alkali metals such as Sodium, Potassium or Lithium
• metals such as Ti ⁇ tane, Iron, Lead, etc.
• ammonium halides can also be used insofar as they are related in their structures and their chemical properties to the corresponding Potasium salts.
• All these salts can be used with varying concentrations according to their specific solubility and electrical conductivity in aqueous or alkaline solution, or possibly in the pure state.
• Sea salt and rock salt can constitute one of the variations of anodic compound which can be used in the generator according to the invention, in so far as they consist mainly of sodium chloride and potassium.
• the low electrical conductivity of seawater requires special arrangements at the level of the anode of the generator if it is used directly.
• the invention relates to batteries, accumulators and electric generators or fuel cells, as follows.
• the element In the category of batteries or accumulators, the element consists of:
• a cathode (positive electrode) composed of a metal oxide, such as titanium dioxide, cobalt oxide, silver oxide, etc. hydroxide and is dissolved in the electrolyte which under these conditions must bathe the cathode to the exclusion of the other constituents of the element, is deposited on a deployed metallic support, laminated or sintered such as Nickel.
• a metal oxide such as titanium dioxide, cobalt oxide, silver oxide, etc. hydroxide
• anode consisting of chloride or more generally a halide of Sodium, Lithium, Calcium, Potas sium, etc. or of a non-alkali metal such as Titanium, Lead, Iron, etc.
• This chloride or, more generally, this halide is either dissolved in the electrolyte at a concentration close to saturation, or impregnated on a metallic support that is good conductor and spongy, such as nickel or titanium, deployed, laminated or sintered, or is molded under high pressure on a metallic conductive support playing the role of current collector.
• an electrolyte which is, depending on the case, an aqueous or alkaline solution, or a mineral or animal gel with high alkalinity, this
• separator which acts as an ion exchange membrane and which consists of raw kaolin porcelain as thin as possible, or of a cellulose compound, or of a synthetic fiber composite nylon or polypropylene, or a car ⁇ boné compound, made non-conductive, these compounds possibly being complemented. tees with an ion-permeable cellophane membrane.
• the positive electrode is composed of one or more metal hydroxides, obtained for example from titanium dioxide and / or Cobalt oxide and / or Silver oxide , etc.
• These metal hydroxides can, in a first variant, be deposited on a metallic support which is a good conductor, deployed, laminated or sintered, or, in a second variant, can be dissolved in the alkaline solution, for example sodium hydroxide or of potash, which bathes the cathode to the exclusion of the other constituents of the generator.
• the cathode is designed to permanently ensure a very close interaction between the air or the oxygen used as oxidant in the electrochemical oxidation reactions, and the metal hydroxide or hydroxides designated above.
• the first variant air or oxygen is introduced and brought into contact with the active materials of the cathode by microperforations carried out. over the entire external surface of the cathode frame and obtained for example by electrical effluvage.
• the metallic hydroxides are dissolved in the alkaline solution
• air or oxygen are introduced into the bath by orifices placed at the bottom of the container and ensuring a permanent erosion of these gases in the solution in view of the reoxygenation of the active materials of the cathode;
• the electric current is collected by an auxiliary conductive metal electrode consisting for example of expanded nickel, rolled or sintered, and whose exchange surface with the cathode solution is as large as possible.
• the alkaline solution of sodium hydroxide or potassium hydroxide, designated above, which plays the role of electrolyte in the generator, can be supplemented with various additives such as lithium oxide, which provide better ion exchange.
• the negative electrode (anode) consists of an alkaline or metallic halide, for example a chloride such as sodium chloride, potassium chloride, or tetrachloride.
• a chloride such as sodium chloride, potassium chloride, or tetrachloride.
• de Titanium dissolved if it is acts as an alkali halide, in an alkali hydroxide or in water.
• Salt in normal or concentrated solution in seawater, naturally constitutes an application of this type of electrode, in a variant corresponding to the use of an aqueous solution.
• This application requires, as already mentioned above, the use of an auxiliary metal electrode intended to collect the current flowing at the level of the anode.
• This collecting electrode is made of an expanded, sintered or laminated metal, offering the widest possible exchange surface with the salt solution in which it is immersed.
• the separator which acts as an ion-exchange membrane between the positive electrode and the negative electrode of the generator, is made up either of kaolin porcelain, or of a cellulosic compound or of a synthetic material based on nylon or polypropylene fibers or on a carbon compound made non-conductive, both being optionally supplemented with a cellophane membrane.
• Titanium dioxide constitutes the basic active material:
• Ti0 2 , 2H 2 ⁇ On contact with air or oxygen introduced into the cathode, the titanium hydroxide (Ti0 2 , 2H 2 ⁇ ) is regenerated as follows: Ti0 2 , 2H 2 0 + 1 0 2 > Ti (0H) 3 00H
• anode solution is, as a variant, constituted of potassium iodide in solution in water or in potassium hydroxide, the corresponding reaction can be written:
• the salt initially contained in water or in the alkaline solution is, in theory, completely oxidized.
• the perchlorate, or more generally perhalogenate, obtained when all or part of the chloride or of the halide has been oxidized can be regenerated if necessary by making it cross the generator again, the polarities then being reversed as when recharging a conventional accumulator.
• This regeneration mode will of course only be usable when all the precautions are taken to avoid concomitantly the phenomena of electrolysis, in particular the regeneration will preferably take place on perhalogenates in high concentrations.
• this device comprises an external cylindrical plastic container 1, to which are connected tubes 2 for admitting the anode liquid, composed, for example, of sodium chloride or of Potassium in alkaline or aqueous solution.
• a valve 3 controls the flow of admission of the anodic liquid into the tank.
• a tube 4 is arranged in the bottom of the tank and makes it possible to ensure the eva ⁇ cuation of the used anode liquid to an external auxiliary recovery tank.
• the anode liquid 5 bathes the auxiliary collector electrode 6 made of expanded or sintered nickel, arranged concentrically at the internal periphery of the plastic container and connected to the terminal
• a frame 7 ensures the mechanical strength of the separator. This consists of a layer of polypropylene fiber 8, applied to the frame 7, and an insulating cellophane film 9 electrically permeable to ions.
• the air or oxygen for permanent regeneration of the cathode is introduced at 10, into the lower part of the generator, by a suitable tube placed longitudinally in the cathode compartment.
• the cathode 11 consists of a sintered nickel plate wound on itself, saturated with titanium dioxide and cobalt oxide hydroxides, and immersed in the alkaline solution 12 serving as electrolyte. The cathode 11 is electrically connected to the positive terminal P of the generator.
• the solution 12 can consist of both the alkaline electrolyte and the metal hydroxides in solution or in suspension constituting the active materials of the cathode, the nickel grid 11 then playing the role of electrode auxiliary for collecting and passing electric current.
• the air or oxygen introduced in 10 in excess and under low overpressure relative to atmospheric pressure circulates longitudinally along the cathode and escapes at 13 through an orifice disposed at the part generator top.
• the air inlet and outlet orifices 10 and 13 can be eliminated, the atmospheric pressure being sufficient to permanently ensure the presence of dissolved oxygen in the solution bathing the cathode.
• the anode and cathode compartments are reversed with respect to the arrangement of the appended figure.
• no tubing for admitting air or oxygen into the cathode compartment is foreseen; in return, the external frame 1 of the generator is icro-perforated over its entire surface to allow free passage of air towards the interior of the cathode compartment without however allowing the passage and the flow of the electrolyte or of the solution that bathes the cathode outwards.
• alkali metal or metal halides used as anodes of the generators according to the invention being oxidized in the form of perhalogenates (perflurates, perchlorates, perbromates or periodates) at the end of the electrochemical reactions the principles of which have been set out above, most of them are chemically stable at temperature
• WIPO. WIIPPOO ambient can be reduced, with liberation of oxygen, compounds of lesser degrees of oxidation.
• This operation can be carried out, for example, with the addition of a deoxygenating catalyst such as manganese dioxide, by heating the mixture.
• the decomposition temperature varies according to the compounds obtained and can be at relatively low levels, especially for perioda and perbro ates.
• thermoelectric or photoelectric type coming from the generator after supplying electrical energy, can in these precise cases be easily regenerated by heating or appropriate thermal or photonic radiation.
• This solution may prove to be advantageous if relatively high cost alkali or metal halides are used, leading to perhalogenates which are difficult to store or to eliminate. in addition, it thus ensures energy conversion of the thermoelectric or photoelectric type, which also opens up another field of application for the types of accumulators and generator described above.
• the characteristics of the batteries, accumulators and generators which are the subject of the present invention can place them at the forefront of batteries and accumulators, generators of electrical energy and energy converters. They can be used for the production of electric power, for the supply of traction chains, permanent or emergency lighting networks, vehicles, machines and various equipments and for the conversion of heat or energy solar electricity.

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• Engineering & Computer Science (AREA)
• Manufacturing & Machinery (AREA)
• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Electrochemistry (AREA)
• General Chemical & Material Sciences (AREA)
• Life Sciences & Earth Sciences (AREA)
• Sustainable Development (AREA)
• Sustainable Energy (AREA)
• Hybrid Cells (AREA)

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Applications Claiming Priority (2)

Publications (1)

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• 1978
  • 1978-07-11 FR FR7820637A patent/FR2431195A1/fr active Granted
• 1979
  • 1979-07-11 WO PCT/FR1979/000062 patent/WO1980000284A1/fr unknown
  • 1979-07-11 JP JP50108579A patent/JPS56501224A/ja active Pending
• 1980
  • 1980-02-25 EP EP79900770A patent/EP0016792A1/fr not_active Withdrawn
  • 1980-03-11 US US06/197,348 patent/US4318968A/en not_active Expired - Lifetime

Non-Patent Citations (1)

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