A METHOD OF MANUFACTURING A BATTERY The present invention concerns the activation of batteries of the hydrogen-storage type.
We have previously described novel platinum group metal ("PGM") interface- activated hydride-forming metallic particles in WO98/50968. Such activated materials particularly show improved performance in batteries in charging and discharging. The methods of activation disclosed therein are effective to deposit a discontinuous or partial deposit of one or more PGMs on hydride-forming metallic particles such as AB5, AB2 or AB. Desirably, hydrogen is introduced into the metal particles, then the hydrogen-loaded particles are contacted with a solution of the PGM and the composition is dehydrogenated. The particles may then be pasted up and made into the hydrogen electrode of a battery in the conventional manner. (Throughout this description and claims, the term "battery" is used as being the commonly used expression instead of "cell".) WO 98/50968 discloses PGM loadings of 0.02 to about 8wt%, preferably from
0.08 to about 2wt%.
It would be desirable to develop methods of activation that are easy and safe to incorporate into conventional battery manufacturing processes and which offer the possibility to minimise the usage of expensive PGMs and avoid the costs associated with the activation step as described in WO98/50968.
Accordingly, the present invention provides a method of manufacturing a battery comprising assembling a hydrogen storage battery using dry hydrogen storage alloy or pasted hydrogen storage alloy to construct a hydrogen storage alloy electrode, filling the assembled battery with electrolyte, and sealing and charging the battery wherein hydrogen is generated at the surface of the hydrogen storage alloy electrode during charging and is stored within the alloy bulk by diffusion, characterised in that the electrolyte comprises one or more reducible PGM precursor compound. The charging procedure generates hydrogen which is stored within the hydrogen storage alloy.
The invention further provides a battery-filling composition comprising an electrolyte of an alkali metal hydroxide, optionally KOH or NaOH, solution in combination with an effective amount of one or more reducible PGM precursor compound. The PGM precursor compounds may be capable of being reduced by hydrogen to metallic PGM form. The PGM precursor compounds may be selected from one or more of Pd, Ru and Pt compounds.
It is believed that the method of the invention permits reduction of the PGM-precursor compound in situ to form discontinuous PGM metal deposits on the hydrogen storage alloy. Accordingly, the actual battery manufacturing method is unchanged, permitting easy integration into conventional manufacturing lines.
Further, it is believed that the PGM precursor will be reduced at the available (i.e. wetted) surface of the hydrogen storage alloy electrode during charging, at the most active sites. Thus the method of the invention permits the activation by PGM of the outer surface of the electrode; this permits a minimisation of PGM usage, and avoids PGM deposits being buried within the electrode. It is believed that activation at the surface is completely adequate since hydrogen diffusion within the bulk of the electrode is extremely fast.
Suitable hydrogen storage alloy electrode materials may be selected from AB5, AB2 or AB battery alloys, e.g. LaNi5, Al doped LaNi5, CeNi5, Al doped CeNis, CaNi5, Mn doped CaNi5, ZrV2, Zr(V0.33Ni0.67)2, TiNMn, Zr doped TiCrMn, Zr doped TiCr2, Co doped TiN2, TiΝi, TiMn, TiFe, TiZr, Ti(MnN) and Ti(MnCr).
Electrodes for hydrogen storage batteries are typically made using either Νi or a PTFE/carbon mix to cause the particles of hydrogen storage alloy to bond under pressure together or to bond under pressure to a substrate such as porous Νi. The Νi or PTFE/carbon mix tends to fill pores between the hydrogen storage alloy particles, thus reducing ingress of the electrolyte comprising PGM precursor compound(s), and promoting the deposition of metallic PGM and reduced PGM compound(s) on the outermost surface of the electrode.
Although it is feasible to fill the battery with electrolyte and separately fill, before or after the electrolyte, with PGM precursor compound, in a particular embodiment, a battery filling composition comprising an alkali metal hydroxide electrolyte solution in admixture with the appropriate quantity of PGM precursor compound is used. Suitable compositions cannot readily be defined in terms of wt%, because of widely different battery designs and requirements but may probably best be described as being sufficient to give a desired PGM loading in terms of mg/m2 of geometric electrode area. Suitably the surface concentration may be in a range equivalent to 0.02 to 2 wt% of PGM in the bulk alloy. Since battery design varies with the intended application from button cell design for high capacity low power applications and wound ("Swiss roll") cells for high power applications, the level of PGM surface concentration will vary with application and intended operating regime. The present invention is flexible enough to permit improved activation across the range of applications, and an appropriate loading for a given battery design and for specific power/charge/discharge requirements may be determined by conventional optimisation techniques.
PGM metal concentrations (rather than precursor compound concentrations) may suitably be in the ranges for the above varied types of battery of 0.2 to 4.0 g/m2 PGM, which might be 0.1 to 2.0 g/m2 for each of two PGMs or some other mix of two or more PGMs. Precursor compounds may be selected for their solubility in the solvent being used for the electrolyte, for example an aqueous medium containing, optionally, KOH or NaOH. Examples include:
Pd(diaminoethane)2Cl2 , also known as Pd(en) Cl2 H2Pt(OH)6 Pt(NO3)2 Ru(NO)(NO3) Ru(NO)Cl The PGM precursor compounds are usually chosen from palladium, ruthenium and platinum systems and may be used singly, in pairs or together. Typical compositions comprise Pd Ru, Pt/Ru and Pd Pt. Of these, in one particular embodiment, the Pd/Ru pair is used with the Pd to Ru ratio range from 1 : 10 to 1 :1.
The invention will now be further described by way of illustration only, by reference to the following working examples.
Various Ru precursors were dissolved in 6M KOH solution. An initial assessment was performed by cyclic voltammetry using a typical AB5 battery alloy as an electrode, and the results plotted in Fig 1. The precursor compounds tested were:
Precursor No. Compound 1 ammonium trisoxalato Ru(III) 2 hydrogen trisoxalato Ru(III) 3 Ru(NO)(NO3) 4 Ru(NO)Cl 5 Ru((NH3)5Cl)Cl 2 6 Ru(NH3)6Cl3
Reviewing the plots, clearly precursor compounds Nos. 3 and 4 look most promising because of their lower overpotential. Similar tests were carried out for Pt (from hexahydroxyplatinic acid) and mixtures of Pt + Ru precursor compounds (from hexahydroxyplatinic acid and potassium ruthenate), and attached plots Figs 2 and 3 show the respective cyclic voltamograms, indicating the reduction peaks for Ru and Pt.
Sample commercial batteries were inoculated with precursor compound-loaded KOH and charged and then discharged. Fig 4 shows a typical discharge curve.