ELECTRIC STORAGE BATTERIES

Abstract: A recombinant lead acid electric storage battery in which the plates in each cell are separated by electrolyte and gas permeable compressible fibrous separator material comprising organic polymeric fibres, the separator material having an electrolyte absorption ratio of at least 100%. The separator is made of microfine polyester fibres and has a wicking action.

Description: ELECTRIC STORAGE BATTERIES TECHNICAL FIELD The present invention relates to lead acid electric storage batteries, and is particularly con- 5. cerned with such batteries of sealed or recombinant type in which the gas evolved during operation or charging is induced to recombine within the battery at the battery electrodes. BACKGROUND ' ART 10. Recombinant lead acid batteries are known. An object of the present invention is to provide such a battery having improved separator characteristics. The invention, although described with reference to batteries, is not restricted to batteries " but is 15.* also applicable to single cells e.g. spirally wound cells, and the claims to batteries thus include single cells within their scope. DISCLOSURE OF THE INVENTION According to the present invention there is 20. provided a recombinant lead acid electric storage battery in which the positive and negative plates in each cell are separated by separators of electrolyte and gas permeable compressible fibrous separator material comprising organic polymeric fibres, the 25. separator material having an electrolyte absorption ratio of at least 100%, the volume E of electrolyte in the battery preferably being at least 0.8 (X+Y) where X is the total pore volume of the separators in the dry state and Y is the total pore volume of . the * SmEJ ζj~ OMPI positive and negative active materials in the dry fully charged state, the battery at least when fully charged having substantially no free unabsorbed electrolyte whereby substantial oxygen gas recombination occurs in 5. the battery at charging rates not in excess of C/20. The ratio of X to Y may be in the range 6:1 to 1:1 e.g. 5.5:1 to 1.5:1 or more preferably. -4:1 to-..1.5:1. The charging rate is desirably kept at- hot greater than C/15 and preferably less- han C/20 e.g. 10. C/20 to C/60. The volume of electrolyte is desirably in the range 0.8 (X+Y) to 0.99 (X+Y) and especially at least 0.9 (X+Y) or even at least 0.95 (X+Y). These •values enable the active material to be utilized more efficiently than when lower amounts of electrolyte are 15. used. We have found that surprisingly oxygen gas recombination can still occur at the negative elec¬ trodes at these very high levels of saturation of the pores which is contrary to what is conventional in 20. recombinant sealed lead acid cells.. The electrolyte active material ratio is at-least 0.05 e.g. at least 0.06 or at least 0.10 and is the ratio of H SO. in grams to the lead in the active material on the positive and negative electrodes cal- 25 * . culated as grams of lead. - 1 - " . OMPI / t o WIPO It is preferably in the range 0.10 to 0.60 especially 0.11 to 0.55 e.g. 0.20 to 0.50. The ratio of negative to positive active material (on a weight of lead basis) may be in the range 0.5:1 5. to 1.5:1 e.g. 0.6:1 to 1.4:1. The use of ratios below 1:1 is contrary to what is conventional but we find that recombinant operation can be achieved at these ratios and" hey have the advantage of providing more positive active material for the same cell volume. 10. We thus prefer to use ratios in the range 0.6:1 to 0.99il.e.g.0.7:1 to 0.9:1. As mentioned above the separator material is a • compressible absorbent fibrous material having an electrolyte absorption ratio of at least 100% e.g. 15. of 100 ' to 200% especially 110 to 170%. It is elee- . trically non-conducting and electrolyte resistant. Electrolyte absorption ratio is the ratio, as a percentage, of the volume of electrolyte absorbed ^ by the wetted portion of the separator material to 20. the dry volume of that portion of the separator mater¬ ial which is wetted, when a strip of the dry separator material is suspended vertically above a body of aqueous sulphuric acid electrolyte of 1.270 SG con¬ taining 0.01% by weight sodium lauryl sulpnonate with 25. 1 cm of the lower end of the strip immersed in the electrolyte, after a steady state wicking condition has been reached at 20 C at a relative humidity of less than 50%. The thickness of the separator is measured with 4 . a micrometer at a loading of 10 kilpascals (1.45 psi) and a foot area of 200 square millimetres (in accord¬ ance with the method of British standard specification No. 3983). Thus the dry volume of the test sample is 5. measured by multiplying the width and length of the sample by its thickness measured as described. We also prefer that the separator material should have a wicking height of at least 5 cms on the above test, namely that the electrolyte should have risen to * 10. a height of at least 5 cms above the surface of the electrolyte into which the strip of separator material dips when the .steady state condition has been reached, • so that good electrolyte distribution is achieved in each cell. 15. We find that these two requirements are met by - fibrous blotting paper-like materials made from poly¬ meric fibres, especially polyester fibres, having diameters in the range 0.01 microns or less up to ' 10 microns, the average of the diameters of the fibres 20. being less than 10 microns, and preferably less than 5 microns, the weight to fibre density ratio, namely the ratio of the weight of the fibrous material in grams/square metre to the density in grams/cubic centimetre of the material from which the individual 25. fibres are made preferably being at least 20 prefer¬ ably at least 30 and especially at least 50. In a preferred .form of the invention the elec¬ trolyte is an aqueous sulphuric acid electrolyte con¬ taining an amount of wetting agent effective to ensure O that the electrolyte wicks up the separator to a height of at least 5 cms in the above test, e.g. an amount of at least 0.01% by weight of sodium lauryl sulphonate, and the separator has thermoplastic 5. organic polymer fibres of diameters in the range up to 10 microns e.g. in the range 1 to 6 microns and the average of the diameters of the fibres is less than 10 microns e.g. 1 to 6 microns especially 1 to 4 microns. 10. Moreover the above combination of properties of the separator gives a material which is highly resistant to "treeing through" , namely growth of lead dendrites from the positive electrode in a cell to the negative electrode producing short circuits, whilst at 15. the same time even when containing large amounts of • absorbed electrolyte, still providing a substantial degree of gas transmission capability. Recombinant lead acid batteries, in which gas recombination is used to eliminate maintenance during 20. use, operate under superatmospheric pressure ' e.g. from 1 bar (atmospheric pressure) upwards and due to the restricted amount of electrolyte, the high elec¬ trolyte absorption ratio of the separator, and the higher electrochemical efficiency of the negative 25. electrode, the battery operates under the so-called "oxygen cycle". Thus oxygen generated, during charging or overcharging, at the positive is trans¬ ported, it is believed, through the gas phase in the separator to the surface of the negative which is -fJRE ^ O PI damp with sulphuric acid and there recombines with the lead to form lead oxide which is converted to lead sulphate by the sulphuric acid. Loss of water is thus avoided as is excess gas pressure inside the battery. 5. The higher electrochemical efficiency of the negative active material enables the negative elec¬ trode to effect recombination of the oxygen produced by the positive electrode even at the beginning of the charge cycle. Thus it may not be necessary to have an 10. excess weight of negative active material compared to the positive active material. However recombinant operation of the battery may ' be facilitated by the use of a number of features in combination. 15. Thus firstly one desirably provides that, under the charge and discharge conditions, under which the battery is designed to operate, the capacity of the negative electrodes in each cell will normally, and desirably always, be-in excess of that of the posi- 20. tive electrodes. ' The electrochemical efficiency of the negative electrodes is in general greater than that of the positive electrodes but it must be born in mind that the efficiency of the negative electrodes drops more 25. rapidly than that of the positive electrodes both as the cells undergo increasing numbers of cycles of charge and discharge and as the temperature of oper¬ ation is reduced below ambient (i.e. 25°C) . Excess negative capacity may thus conveniently be ensured 30. by providing an excess of negative active material (calculated as lead) compared to the positive active material in each cell. Secondly one provides a restricted amount of electrolyte as described above and thirdly one pro- 5. vides a separator, having a high electrolyte absorp¬ tion ratio as also described and defined above, which is compressible, so as to conform closely to the surfaces of the electrodes, and which has wicking or capillary activity, hereby transmission of elec- 10. trolyte and electrolytic conduction between the electrodes is facilitated and preserved independent of the orientation of the cell, whilst gas transmission • through the open spaces in the separator is maintained ^ so that adequate and rapid gas transmission between the 15. electrodes is also ensured. Use of a fibrous seperator having very small fibre diameters ensures that the open spaces in the separator are highly tortuous thus fulfilling the requirement that the separator resist "treeing through" as des- 20. cribed above. If the charging conditions generate oxygen at a faster rate than it can be transported to the negative and react thereat, then the excess oxygen is vented from the battery. 25. The container of the battery is thus provided with gas venting means. The gas venting means preferably take the form of a non-return valve so that air cannot obtain access to the interior of the battery although excess 30. gas generated therein can escape to atmosphere. The lid of the container may be formed with filling apertures to permit electrolyte to be intro¬ duced into each cell. The filling apertures may be closed after the electrolyte has been added but the 5. closures should provide gas venting means or separate gas venting means should be provided. The surface pore size of the separator can also be controlled, and thereby the resistance of-the separator to "treeing through", by applying a light 10. elevated temperature overall consolidation to one surface of the material to achieve partial fusion of the thermoplastic organic polymer fibres to each other immediately adjacent to the surface without significant consolidation in the body of the separa- 15. tor. Clearly this surface fusion must not be such - as to destroy the. porosity of the surface, merely it must reduce the pore size of the surface. The calendering at the surface of the separator reduces the porosity of the separator at that surface 20. which can be placed in proximity to the positive plate and thus reduces the tendency for "treeing through" to occur. The overall reduction in thick¬ ness of the separator is preferably such that the thickness is at least 40% e.g. 70 to 90% or 99% of the 25. original thickness of the unconsolidated material, which may have been 0.6 to 2 mm or more. The thermoplastic organic polymer fibres may be subjected to an oxidative treatment prior to being formed into the sheet material. OM *«_. wIπP- The oxidative process in designed to increase the wettability of the fibres. This improves the prop¬ erties of the battery separator itself. The oxidative process can consist of or include 5. treatment of the fibres, e.g. of polyolefin with ■.-A-" "' chromic acid, nitric acid, nitric acid-hydrochloride acid blends such as aqua regia, hypochlorite, perman¬ ganate, chlorosulphonic acid, or hydrogen peroxide, or ozone or ultraviolet radiation and this latter 10. agent can be used in conjunction with the other agents, Gas phase chemical treatments e.g. by corona dis¬ charge, or with ozone or ultraviolet light can also be used to increase the wettability of the fibres. Other.chemical treatments effective to increase 15. the wettability of the polymeric fibres can also be • used, for example gas phase exposure to halogens and sulphur dioxide, carbon monoxide or carbon dioxide in sunlight or ultraviolet light or other ionizing radiation to achieve halosulphonation or halocarboxy- .20. lation of the fibres. The fibres must then be sub¬ jected to hydrolysis and substantially complete, elimination of ions liable to interfere with the electrochemical process in the battery for example halogen ions and heavy metal ions such as chromium; 25. this can be achieved by washing. It is preferred however to use oxidative techniques which do not introduce interfering ions. Whilst the preferred oxidative techniques reduce the need for wetting agents it may be desirable to incorporate certain selected wetting agents to reduce the internal resist¬ ance of the separator. We prefer to use sulphonates such as alkyl aryl sulphonates, for example, sodium dodecyl benzene sul- 5. phonate, or succinates such as sulphosuccinates, for example sodium dioctyl sulphosuccinates , or quaternary ammonium wetting agents such as alkyl aryl alkyl quaternary ammonium chlorides. BEST MODE OF CARRYING OUT THE ' INVENTION 10. The invention may be put into practice in various ways and one specific embodiment will be described by way of example to illustrate the invention with ' reference to the accompanying drawings, in which:- Figure 1 is a partial cross-sectional side 15. elevation of part of a starting, lighting and ignition - battery in accordance with the present invention; Figure 2 is an end elevation on the line II-II of Figure 1; Figure 3 is an electron scanning photomicrograph 20., - of a preferred separator material at 200 fold magnifi¬ cation; and Figure 4 is a view similar to Figure 3 at 1000 fold magnification. Example 1 25. The battery has a capacity of 30 Ahr and has six cells accommodated in a container 2 made as a single moulding of polypropylene plastics material and separated from each other by integral intercell partitions 4. The cells are sealed by a common lid 30. 6 which is connected to the walls of the container 2 OMP at 7 and the partitions 4 at 8 by the method known as "heat sealing" in which the edges to be joined are placed in contact with opposite surfaces of a heated tool which is subsequently withdrawn and the 5. partially melted edges are pressed together. Each cell contains four positive plates 10 inter¬ leaved with five negative plates 12 separated from one another by separators 14 consisting of four layers of electrolyte and gas permeable compressible 10. polyester fibre mat material whose composition and function will be described below. A double sheet of separator 14 is also placed on both outside faces • of each cell. The positive plates 10 and negative plates 12 are formed from a cast grid of lead alloy 15. containing 0.07% calcium and 0.7% tin" and carry positive and negative active electrode material res¬ pectively. The positive plate is 2.0 mms thick and the negative plate is 1.8 mms thick and are held in inti- 20. mate contact with the separators by solid polypropy¬ lene packing pieces 30. Both faces of all plates are covered by separator material, which extends out above and below and on each side of the plates. More broadly the plates may be 1 to 2 mms e.g. 25. 1.2 to 1.9 or 1.2 to 1.6 mms thick. The positive active material had the following composition before being electrolytically formed: Hardinge grey oxide 13640 parts, fibre 6 parts, water 1800 parts, 1.40 SG aqueous sulphuric acid 750 -parts. The paste had a density of 4.2 gr/cc. The negative active material had the following composition before being electrolytically formed: Hardinge oxide 13640 parts, fibre 3 parts, barium 5. sulphate 68 parts, carbon black 23 parts, stearic acid 7 parts, Vanisperse CB (a lignosulphonate) 41 parts, water 1525 parts, 1.40 SG aqueous sulphuric acid 875 parts. The paste had a density of -4.3. Vanisperse CB is described in British patent 10. specification No. 1,396,308. As the active material has sulphuric acid added to it, its porosity decreases. When the active ' material is- charged its porosity increases and in the fully charged condition is about the same as it 15. is in the unformed state* before addition of electro¬ lyte. Each positive plate carried 109 grams of active material on a dry weight basis. . Each negative plate carried 105 grams of active 2β . material on a dry weight basis. Each sheet of the ' separators 14 is a highly absorbent short staple fibre polyester matting, about 0.3 mm thick, there being fibres 61 as thin as 1 micron and fibres 60 as thick 25. as 6 microns in diameter, the average of the dia¬ meter of the fibres being about 2.0 microns. Figures 3 and 4 show this material at different magnifications, Figure 3 at 200 fold and Figure 4 at 1000 fold. It will be observed that the material whilst highly absorbent still has a very large amount of open space between the individual fibres. The material when tested for its wicking and electrolyte absorption capabilities by being suspended vertically above a 5. body of sulphuric acid of 1.270 SG containing 0.01% by weight of sodium lauryl sulphonate with 1 cm of its end dipping in the electrolyte in an atmosphere of 20°C and a relative humidity of less than 50% absorbs elec¬ trolyte so that the liquid has wicked up to a height o-f 10. 5 cms after 2 hours and this is the steady state condition. This 5 cms of material absorbs 132% of its own dry volume of electrolyte, and this is its electro- • lyte absorption ratio. Each sheet of the separator 14 weighs 50 grams/ 15. square metre and has a porosity of about 90% as . measured by mercury intrusion penetrometry. The density of the polyester from which the fibres of the separator are made is 1.32 gr/cc; the weight to fibre density ratio is thus 39 for each sheet or 151 for the 20. complete separator. Each sheet of separator material is 0.3 mms thick and weighs 50 grams/square metre. The total volume of separator used for each cell is 238 cc which has a pore volume of 214 cc and a porosity of 90% before 25. being placed in the cell. When in the cell the volume of separator is 218 cc and the pore volume is 183 cc. This is the value of X. The weight of separator present in each cell is 42 grams. The electrical resistance of the 0.3 mm thick 30. separator was measured by placing it between two flat OMPI lead sheets having an area of 25.1 square cms immersed in the above electrolyte and allowed to soak for hour, 2 hours and 24 hours before measuring the resistance in milliohms. The values were 3.5, 1.5 and 1.0 but without 5. the wetting agent the values were 296, 8.0 and 1.5. The separators being compressible conform closely to the surfaces of the plates thus facilitating electrolyte transfer and ionic conduction between the plates via the separator. 10. The total geometric surface are of the positive plates in each cell.is 767 square centimetres and of the negative plates 959 square centimetres. The dry weight of active material of the positive plates is 4 x 109 x 1.07 i.e. 468 grams (as Pb0 2 i.e. 405 grams 15. as lead * ) and that of the negatives is 5 x 105 x 0.93 • i.e. 490 grams (as lead) an excess of 4.7% negative active material based on the weight of the positive active material (21% as lead). The total weight of the grids is 763 grams. 20. The true density of the positive active material (Pb0_) in the fully charged state is 9 gr/cc and the true density of the negative active material (sponge lead) in the fully charge state is 10.5 gr/cc. The true volume of the posiτive active 25. material is 4 x 109 -J- 9 i.e. 48.4 ccs and the true volume of the negative active material is 5 x 105 10.5 i.e. 50 ccs. The apparent density of the dry positive active material is 4.2 gr/cc and thus the apparent volume of the dry positive active material is 4 x 109 τ 4.2 i.e. 103.8 ccs. The apparent density of the dry negative active material is 4.4. gr/cc and thus the apparent volume of the dry negative active material 5. is 5 x 105 4.4. i.e. 119.3 ccs. Thus the pore volume of the positive active material is 55.4 ccs and of the negative active material is 69.3 ccs and the total pore volume of the dry fully charged active material is 124.7 ccs, which' 10. is the value of Y. The ratio of X to Y is 1.47:1. (X+Y) is 307.7. The calculated true surface area for the posi¬ tive active material is 1170 square metres and for the negative is 220 square metres using a factor of 15. 0.45 square metre/gram for the negative active mater¬ ial and 2.5 square metres/gram for the" positive active material. Each dry electrolytically unformed cell was evacuated to a high vacuum and had 325 ml i.e. 1.06 20. (X+Y) of 1.275 SG aqueous sulphuric acid (i.e. 153 grams of sulphate ion) added to the unformed cell. The cells were then allowed to cool to 40°C (1 to 2 hours) and electrolytically formed and 34.5 cc of water was electrolysed off, the specific gravity 25. of the electrolyte thus rising. The electrolytic forming regime comprised: 4 hours at 11 amps, 17 hours at 5.5 amps, 7 hours at 2.7 amps and 20 hours at 2.2 amps. The amount of electrolyte remaining is thus 0.94 30. (X+Y). O PI ^ τ° o The battery contained 0.7 ml of 1.275 SG aqueous sulphuric acid per gram of positive active material (as lead) and 0.66 ml of 1.275 SG aqueous sulphuric acid per gram of negative active material as lead. The battery contained 0.34 ml of 1.275 SG aqueous sulphuric acid per gram of positive and negative active material combined (as lead).. There were thus 0.4 grams of H_S0 u per gram of lead in the positive active material and 0.35 grams 10. of H S0^ per gram of lead in the negative active material. The electrolyte active material ratio was thus 0.18. The battery was then tested on the following test regime and completed this regime. 15. 4 Cycles at C/5, namely discharge at 20°C at 8.8 amps to an end voltage of 10.2 volts followed by recharging at 14.1 volts for 24 hours. 2 Cycles of C/20 discharge, namely discharge at 20°C at 2.2 amps to an end voltage of 10.5 volts 20. followed by recharging at 14.1 volts for 24 hours. 1 Cycle of discharge at -18°C at 220 amps to an end voltage of 6 volts followed by recharging at 14.1 volts for 24 hours. 1 Cycle of C/20 discharge. 25. 1 Cycle of discharge at -18°C as above. The positive and negative plates are inter¬ connected by a respective positive and negative group bar 16 and 18. Integral with the negative group bar 18 in the right hand cell as shown in Figure 1 is a 5. laterally projecting portion which terminates in a "flag" or upstanding portion 20 which is adjacent to the intercell partition 4 and overlies a hole 22 in the partition.. The positive flag in the left hand of the two cells shown in Figure 1 is connected to the 10. similar negative flag in the right hand cell through the hole 22 so as to form an intercell connection by a method known as "extrusion fusion". This method comprises placing welding jaws against the two opposed flags before the lid 6 is placed in position, 15. applying pressure so that the flags distort and meet in the hole 22 and fhen passing an electric current between the two welding jaws so that the material of the two flags is melted together and seals the hole 22. -20. The positive group bar in the right hand cell is provided with a flag 24. The flag 24 is connected to a terminal 26 in the lid of the con¬ tainer. Each cell of the battery is normally sealed, 25. that is to say that during normal operation of the battery the cells do not communicate with the atmos¬ phere. However in case a substantial over-pressure should build up in the cell, for instance because the cell is exposed to a very high temperature or OMPI over-charged, so that oxygen gas is evolved at a faster rate than it can be combined, a relief valve is provided to exhaust the excess gas and is arranged to operate at a pressure of only 2 to 3 psi. Each 5. valve is of the Bunsen type and comprises a passage 36 communicating with the interior of a cell and leading to the exterior of the lid. Each passage 36 is within a boss in a respective recess 38 in the lid, and the boss is sealingly covered by a resilient cap 10. 40 having a depending skirt around the boss. The cap 40 normally seals the passage 36, but if an excessive pressure should occur in the battery the skirt of the •cap lifts away from the boss to vent the cell. A disc 42 provided with a vent hole or clearance and 15. keyed into the under cut top edge of the recess 38 engages each cap 40., thus ensuring that it is not blown off by the gas pressure, whilst allowing venting to atmosphere. Example 2 20. The battery is an automotive starting, lighting and ignition battery and is of the same structure as that described and illustrated for Example 1. . However the battery has a capacity of 25 Ahr and each of the six cells contains 3 positive plates 10 inter- 2 * 5. leaved with 4 negative plates 12 separated from one another by separators 14 consisting of 2 layers of electrolyte and gas permeable compressible polyester fibre material whose composition and function will be described below. A single sheet of separator 14 _ O Λ, ~ W fi Af is also placed on both outside faces of each cell. The positive plates 10 and negative plates 12 formed from a cast grid of lead alloy containing 0.07% cal¬ cium and 0.7% tin and carry positive and negative 5. active electrode material respectively. The positive and negative plates are both 1.37 mms thick. The positive and negative active materials are the same as in Example 1. 10. Each positive plate carried 76 grams of active material on a dry weight basis. Each negative plate carried 76 grams of active • material ona dry weight basis. Each sheet of the separators 14 is a highly 15. absorbent short staple fibre polyester matting having a structure and properties as described in Example 1 but being about 0.6 mms thick. Each sheet of the separator 14 weighs 100 grams/ square metre and has a porosity of about 90% as 20. measured by mercury intrusion penetrometry. The density of the polyester from which the fibres of the separator are made is 1.32 gr/cc; the weight to fibre density ratio is thus 78 for each sheet or 151 for the complete separator. 25. Each sheet of separator material is 0.6 mms thick and weighs 100 grams/square metre. The total volume of separator used for each cell is 155 cc which has a pore volume of 140 cc. and a porosity of 90% before being placed in the cell. When in the 30. cell the volume of separator is 140 cc and the pore volume is 126 cc. This is the value of X. The weight of separator present in each cell is 25 grams. The total geometric surface area of the positive plates in each cell is 500 square centimetres and of 5. the negative plates 667 square centimetres. The dry weight of active material of the positive plates is 3 x 76 x 1.07 i.e. 244 grams (as PbO i.e. 211 grams as lead) and that of the negatives is 3 x 76.x 0.93 i.e. 282 grams (as lead) an excess of 15% negative 10. active material based on the weight of the positive active material (34% as lead). The total weight of the grids is 350 grams. The pore volume of the positive active material is 29.3 ccs and of the negative active material is 15. 40.0 ccs and the total pore volume of the dry fully charged active material is 69.3 ccs, which is the value of Y. ' The ratio of X to Y is 1.81:1. (X+Y) is 195.3. The calculated true surface area for the positive 20. active material is 570 square metres • and for the negative is 137 square metres using a factor 0.45 square metre/gram for the negative active material and 2.5 square metres/gram for the positive active material. Each dry electrolytically unformed cell was 25. evacuated to a high vacuum and had 230 ml i.e. 1.18 (X+Y) of 1.275 SG aqueous sulphuric acid (i.e. 108 grams of sulphate " ion) added to the unformed cell. The cells were then allowed to cool to 40 C (1 to 2 hours) and electrolytically formed and 20 cc of water was 30. electrolysed off, the specific gravity of the electro- lyte thus rising. The electrolytic forming regime comprised: 48 hours at 2.5 amps. The amount of electrolyte remaining is thus 1.08 5. (X+Y) and would thus appear by calculation to exceed the pore volume of the system in the fully charged state. The plates and separator are thus very nearly saturated but since no venting occurs there must be 10. sufficient gas space in the separators and plates at least at conditions approaching full charge for gas phase (oxygen) transport to be occurring at this rate ' of charging. The battery contained 1.0 ml of 1.300 SG aqueous 15. sulphuric acid per gram of positive active material • (as lead) and 0.75 ml of 1.300 SG aqueous sulphuric acid per gram of negative active material as lead. The battery contained 0.42 ml of 1.300 SG aqueous sulphuric acid per gram of positive and negative 2.0. active material combined (as lead). There were thus 0.52 grams of H„S0 u per gram of lead in the positive active material and 0.39 grams of H SO. per gram of lead in the negative active material. The electrolyte active material 25. ratio was thus 0.22. 5 Cells of the above design were over-charged for 900 hours at a rate of C/12 namely 2 amps con¬ stant current. After 48 hours the cells had each lost between 9.6 and 13.5 ccs of water when on a 30. Faradaic basis one would have exDected them each to have lost 31 ccs. After 144 hours they had each lost a total of between 14.9 and 19.3 ccs ' of water i.e. about a further 5 ccs when on a Faradaic basis one would have expected them each to have lcs-t 72.6 5. ccs (a further 31 ccs). After 288 hours they had each lost a total of between 17.2 to 23.6 ccs (Faradaic loss 192 ccs). After 678 hours they had each lost a total of between 25.6 and 30.7 ccs (Faradaic loss 452 ccs). After 900 hours they had 10. each lost a total of between 26 and 31 ccs (Faradaic loss 600 ccs). Thus over the 900 hour period the cells exhibited a recombination efficiency of 95 to 96%. Reference has been made above to cast lead alloy . 15. grids. Whilst this is preferred the electrode pairs could be made from slit expanded sheet or be of wrought form e.g. perforated or punched sheet or from •fibrous supports provided with * electrically conduc¬ tive coatings or deposited conductors such as are 20. disclosed in the present applicants -British appli¬ cations Nos. 9876/76 and 15663/76. The grids are preferably 0.1 to 3.0 mms thick especially 1.5 to 2.5 mm thick. The preferred alloy is a lead calcium tin alloy preferably containing 0.06 to 0.13% e.g. 25. 0.07 to 0.09% calcium and 0.3 to 0.99% tin e.g. 0.4 to 0.8% tin e.g. 0.07% calcium and 0.7% tin. Alternative 'alloys include 99.9% lead and anti- monial alloys such as those disclosed in United States patents Nos. 3879217 and 3912637. O PI Due to the fact that the cells rarely if ever communicate with the atmosphere, the battery will not need topping up with electrolyte and is therefore maintenance free. Furthermore the battery is unspill- 5. able firstly because it is sealed and secondly because there is substantially no free electrolyte in the cells, the electrolyte being retained within the microfine separators and the active material. The fact ' that the cells are sealed also means that no spark or explosion ' 10. can propagate from the atmosphere into the battery or vice versa. INDUSTRIAL APPLICABILITY The invention is applicable to recombinant lead acid electric storage batteries and cells.

Claims: CLAIMS 1. A recombinant lead acid electric storage battery in which the positive and negative plates in each cell are separated by separators of electrolyte and gas permeable compressible fibrous separator material comprising organic polymeric fibres, the separator material having an electrolyte absorption ratio of at least' 100%, the battery at least when fully charged having substantially no free unabsorbed electrolyte whereby substantial oxygen gas recombin¬ ation occurs in the battery at charging rates not in excess of C/20. 2. A battery as claimed in Claim 1 in which the volume E of electrolyte in the battery preferably being at least 0.8 (X+Y) where X is the total pore volume of the separators in the dry state and Y is the total pore volume of " the positive and negative active materials in the dry fully charged state. 3. A battery as claimed in Claim 1 or Claim 2 in which the separator material has a wicking height of at least 5 cms on the test defined herein, namely that the electrolyte should have risen to a height of at least 5 cms above the surface of the electrolyte into which the strip of separator material dips when the steady state condition has been reached. 4. A battery as claimed in Claim 1 or Claim 2 in which the separator is a fibrous blotting paper- - uREA OMPI IPO like material made from polymeric fibres having diameters in the range 0.01 microns or less up to 10 microns, the average of the diameters of the fibres being less than 10 microns, the weight to fibre density ratio, namely the ratio of the weight of the fibrous material in grams/square metre to the density in grams/cubic centimetre of the material from which the individual fibres are made, being at least 20. 5. A battery as claimed in Claim 1, 2, 3 or 4 in which the '.electrolyte is an aqueous sulphuric acid electrolyte containing an amount of wetting agent effective to ensure that the electrolyte wicks up the separator to a height of at least 5 cms in the wicking test defined herein. 6. A battery as claimed in any one of Claims 1 to 5 in which the surface pore size of the separator is reduced by applying an elevated temperature overall consolidation to one surface of the material to achieve partial fusion of the thermoplastic organic polymer fibres to each other immediately adjacent to the surface without significant consolidation in the body of the separator. 7. A battery as claimed in any one of Claims 1 to 6 in which the"separator incorporates an alkyl aryl sulphonate, a sulphosuccinate or a quaternary ammonium wetting agent. 8. A battery as claimed in Claim 7 in which the wetting agent is sodium dodecyl benzene sulphonate, sodium dioctyl sulphosuccinate or an alkyl aryl alkyl quaternary ammonium chloride.

Inventors: CULPIN B, PETERS K
Applicants: CHLORIDE GROUP LTD, CULPIN B, PETERS K
Application year: 1980
Main classification: H01M10
IPC codes: H01M10