Electrochemical cell

Abstract: Electrochemical cell comprising a negative electrode consisting of a substrate made of porous material which is impregnated with an electrochemically active material (15, 16), the electrochemically active material being an intermetallic compound which forms a hydride with hydrogen, highly efficient and high-speed gas reactions occurring at the electrode because of the fact that the substrate is impregnated in accordance with a pattern such that a portion of substrate surfaces contains free metal (14).

Description: The invention relates to an electrochemical cell comprising a positive electrode of nickel hydroxide and a negative electrode consisting of a substrate made of porous nickel which is impregnated with an electrochemically active material being an intermetallic compound which forms a hydride with hydrogen, and an aqueous alkaline electrolyte. Examples of the use of electrochemical cells comprising such an electrode are fuel cells and sealed rechargeable cells. Philips Journal of Research, Vol. 39, Suppl. No. 1, 1984 (Eindhoven, NL), pages 71-90, discloses a nickel-hydride cell having a negative electrode consisting of a nickel substrate which is coated with a paste of electrochemical active material, i.e. an intermetallic compound which forms a hydride with hydrogen. The nickel substrate is uniformly coated with the active material and there is no free nickel at the surface. French Patent Application FR-A-2365215 discloses a nickel cadmium cell in which the negative cadmium electrode is partly covered with a catalyst metal in order to promote the recombination of hydrogen gas evolved at the positive electrode with the cadmium electrode during overdischarge of the cell. In several types of electrochemical cells reactions occur at the interface of a solid electrode, a liquid electrolyte and a gas present. This is, for example, the case in several types of fuel cells, but also in sealed rechargeable cells. In a gas-tight rechargeable nickel-metal hydride cell oxygen recombination occurs at the negative electrode during excessive charging of the cell. In such a cell hydrogen generation occurs at the positive electrode during excessive discharging of the cell. It is desirable for the recombination reactions to proceed as rapidly as possible, for a fuel cell, because of the cell efficiency and for rechargeable cells because of their operating life, expressed in charging and discharging cycles. When in a rechargeable cell the recombination rate on charging or discharging is insufficient, the pressure in the cell increases. This may cause gas (possibly with electrolyte) to escape via a safety valve, which reduces the operating life and the capacity of the cell. The invention has its object to provide an electrochemical hydride cell, in which gas reactions occur at the electrode with high efficiency and at a high rate. The invention has more specifically for its object to provide a rechargeable cell with a long operating life, which may however not be obtained at the cost of the initial capacity and the loadability. According to the invention, this object is achieved by an electrochemical cell of a type defined in the opening paragraph, characterized in that both sides of the substrate are impregnated in accordance with a pattern resulting in adjacent hydrophilic and hydrophobic regions across the whole surface of the negative electrode. An electrode with locally very advantageous recombination properties is obtained when the substrate is a flat plate wherein portions are present which at both sides are not impregnated, this being maintained during further processing operations on the electrodes, for example on rolling or further steps in which the electrodes are given their appropriate shapes. A suitable, simple method of producing an electrochemical cell according to the invention, is characterized in that the electrode is produced by partly wrapping a non-porous material in the form of tape around the substrate, whereafter the electrochemically active material in paste form is pressed into the porous substrate, whereafter the tape material is removed. The rate at which the above-mentioned interface reactions proceed depends inter alia on the size of the catalytic surface area present, i.e. the free metal surface of an electrode contacted by the gas. The quantity of active material which is decisive for the capacity of the cell must consequently not be too large. In addition there is the fact that, when a cell contains an excessive quantity of electrolyte or when the electrolyte is preferably bound by the electrode, the free metal surface is covered with liquid as a result of which the gas recombination rate is significantly reduced. On designing a, for example, gas-tight rechargeable cell, compromises must be made between a high gas recombination rate, a high loadability and a large capacity. This constitutes a problem, more specifically for cells having a nickel/nickel hydroxyde electrode as its positive electrode and a hydride-forming intermetallic compound as its negative electrode, since in such a cell no water transport takes place during the charging and discharging cycle. As a result thereof a mechanism which might ensure that the electrolyte periodically disappears from the electrodes is missing. According to the invention, this problem is solved by producing an electrode having both hydrophilic and hydrophobic regions. Gas recombination requires pores in which gas, electrolyte and metal contact each other, and that is optimally the case on a surface having a transition from a hydrophilic to a hydrophobic character. Thus, the water produced during oxygen recombination will, for example, not cover the free, active surface but will be conveyed to a more hydrophilic region. The invention is based on constructing an electrode which is locally very suitable for gas recombination reactions and in other places behaves as a suitable electrode for a rechargeable cell. By separating these functions, better properties are obtained then with an electrode which evidences the same compromise properties over the entire surface area. In addition, any changes in the hydrophilic character of the electrode during the operating life of a rechargeable cell will have no or a much lower influence on the gas recombination rate. The invention and its advantages will now be described in greater detail with reference to embodiments and an accompanying drawing, in which Figure 1 is a partially cross sectional and partly elevational view of a sealed rechargeable electrochemical cell according to the invention, and wherein Figure 2 is a schematic elevational view of a specific construction of an electrode for use in a cell according to the invention. Example of a state of the art rechargeable cell structure The cell which is shown in Figure 1 and which is sealed from the air is made from a suitable housing 1 made of metal, for example stainless steel and provided with a cover 2 having apertures for the conductors 3 and 4. By means of synthetic resin material rings 5 the conductors are insulated from the metal housing (1,2). At the outside the housing may have, for example, a diameter of 22 mm and a height of 41 mm. A wound section consisting of a negative electrode 6, a separator 7 and a positive electrode 8 is provided within the housing, whilst the whole assembly is enveloped by an electrically insulating plastic film 9 of, for example, polyvinyl chloride and bears on a disc 10 made of an electrically insulating material, for example polyvinyl chloride. The negative electrode 6 comprises a hydride-forming intermetallic compound and is connected to the conductor 3. The hydride-forming compound has, for example, the composition La 0.8 Nd 0.2 Ni 2.5 Co 2.4 Si 0.1 . Further suitable hydride-forming compounds are described in, for example, United States Patent US 4487817. The negative electrode 6 is produced by fusing appropriate quantities of the relevant elements and pulverizing the intermetallic compound thus obtained and by applying it to a nickel substrate, for example with the aid of a polymer binder material such as polyvinylalcohol. The paste is, for example, composed of 75% by weight of the intermetallic compound, 24.5% by weight of water and 0.5% by weight of polyvinyl alcohol. The positive electrode 8 is a nickel hydroxide electrode of the conventional sintered type, and is connected to the conductor 4. An aqueous 6 N potassium hydroxide solution is used as the electrolyte. The electrolyte is absorbed in the separator 7 and is so contacted with the electrochemically active material of the two electrodes that it is wetted thereby. The separator is in the form of a non-woven sheet of polyamide fibres. The free gas space in the cell is approximately 5 cm³. A sealed cell of this type has an EMF of between 1.2 and 1.4 V. The cells in accordance with the invention can be assembled in a conventional manner to form batteries comprising, for example, a plurality of series-arranged cells. It is possible to use the electrode improved in accordance with the invention in electrochemical cells other than the cells described in the foregoing. The cell may be in open connection with the atmosphere or may be sealed from the atmosphere. A cell sealed from the atmosphere may include a valve of such a dimension that it is made operative at a predetermined pressure. In a rechargeable cell of the sealed type the electrochemical active portion of the positive electrode is made of, for example, nickel hydroxide, silver oxide or manganese oxide, nickel hydroxide generally being preferred for practical reasons. The electrolyte used in the cell generally consists of a solution of one or more alkaline metal hydroxides, such as lithium hydroxide, sodium hydroxide and potassium hydroxide, having a pH exceeding 7. In addition, the cell may include a separator which electrically insulates the electrodes, but permits ion and gas transport. The separator may consist of (woven or non-woven) synthetic resin material fibres, for example polyamide fibres or polypropylene fibres, and preferably has a hydrophylic character. An improvement of the negative electrode will be described in the following embodiment. Embodiment An electrochemically active material for the negative electrode of the composition La 0.8 Nd 0.2 Ni 2.5 Co 2.4 Co 2.4 Si 0.1 is prepared by mixing, fusing and pulverizing by means of repeated hydrogen adsorption and desorption of the required quantities of the different compounds. Thereafter the resultant material which with hydrogen is capable of forming a hydride is mixed with a binder, for example polyvinyl alcohol, which results in a paste. It is possible to substitute, for example, methyl cellulose for polyvinyl alcohol. Figure 2 shows an embodiment of a negative electrode for use in an electrochemical cell in accordance with the invention. A synthetic resin tape, having, for example, a width of 3 mm is helically wound around a plate or foil of porous nickel metal. Normal commercially available adhesive tape is suitable for this purpose. Thereafter both sides of the nickel foil are impregnated with the pastes by applying the paste to the foil and by subsequent rolling of the assembly to, for example, a thickness of 0.5 mm. This results in the foil having regions 15 which are impregnated on both sides with electrochemically active material, but also regions 14 which are not impregnated at all. Between these regions there are regions 16 which contain electrochemically active material at one side. Thereafter the synthetic resin tape is removed and the electrode is ready for building into an electrochemical cell. For the production of electrodes impregnated in accordance with a pattern, different suitable masking techniques or silk screening techniques may alternatively be used. A speckled pattern may be chosen for this purpose. It is alternatively possible to choose a striped pattern, for example horizontal or vertical stripes, to promote gas transport in a desired direction. At a cell produced in accordance with this example it was measured after 25 charging and discharging cycles that the pressure in the cell amounts to 0.15 MPa after 24 hours charging, both at a charging rate of 10% and at a charging rate of 20% of the capacity of the cell per hour. Comparative example, not in accordance with the invention . A cell is produced in the manner as described for the embodiment 2, the difference being that during impregnation no tape was wound around the porous nickel metal. The electrode is fully impregnated and has no free metal surface. Measurements on this cell which was not produced in accordance with the invention showed that after 25 charging and discharging cycles the pressure in the cell is 0.50 and 0.80 MPa after 24 of hours of charging, at charging rates of 10% and 20%, respectively, of the capacity of the cell per hour. The electrochemical cells according to the invention have a high capacity and loadability and a long operating life, that is to say they can be charged and discharged a large number of times, without a reduction in their serviceability. More specifically, the operating life is hardly negatively affected by overcharging or overdischarging at high rates. The examples specifically refer to electrochemical cells where hydride forming materials are employed as electrochemically active material for one of the electrodes.

Claims: An electrochemical cell comprising a positive electrode of nickel hydroxide and a negative electrode consisting of a substrate made of porous nickel which is impregnated with an electrochemically active material being an intermetallic compound which forms a hydride with hydrogen, and an aqueous alkaline electrolyte, characterized in that both sides of the substrate are impregnated in accordance with a pattern resulting in adjacent hydrophilic and hydrophobic regions across the whole surface of the negative electrode.

Inventors: FRENS GERRIT, VAN BEEK JOHANN REINER G C M, FRENS, GERRIT, VAN BEEK, JOHANN REINER G. C. M.
Applicants: PHILIPS ELECTRONICS NV, PHILIPS ELECTRONICS N.V.
Application year: 1988
Main classification: H01M4
IPC codes: H01M4, H01M10