The lead-acid battery is one of the oldest commercial rechargeable batteries. In 1859, French physicist Gaston Plante demonstrated the battery's working principle by submerging two lead plates in sulfuric acid. The potential for commercialization was realized only 20 years later, when improvements to the technology were made in using pasted plates that allowed the battery to be discharged and charged through a reverse current1.
Even in the early stages of the invention, the significance of the exposed surface area and the porosity of the battery material became evident. It was understood that the larger the surface area of the material, the greater the battery's capacity2. At the time, the commercialization of the battery found a unique application in the emerging automotive industry1, enabling the starting of internal combustion engines of not only passenger vehicles but also larger engines that were used in the military, such as tanks and airplanes3,4,5.
As the manufacturing technologies improved over the years, so did the advancements in chemical analysis and the understanding of the processes that occur within the battery. There will always be a need to improve the manufacturing process to ensure a consistent product that is not only price competitive but also of good quality and that can provide electrical backup for longer periods of time.
The chemistry that occurs in the battery, referred to as a double sulphate theory, is unique when compared to other battery types. In this case, the electrolyte or acid forms part of the reaction mechanism during the discharge and charge process6.


Figure 1: Schematic illustration of the charging and discharging reaction mechanisms of a lead-acid battery. Please click here to view a larger version of this figure.
Here, the electrodes or plates that can conduct electricity react with the acid to form lead sulphate, which can be seen as an insulator (Figure 1). Not all the material that is on a plate is used in the discharge process. The electrochemical reaction predominantly occurs at the surface of the material that is exposed to the acid, and when the battery is charged, the insulating lead sulphate material then converts back to the conductive lead dioxide and lead on the two plates that are referred to as the cathode and anode, respectively5. The larger the surface area, the more discharge reactions can take place and the more capacity can be obtained. Plates are designed to be relatively thin and usually specific to the application. For high power over short periods of time, as in the starting of a car, a large area is desirable where the acid can easily travel or diffuse to the middle of the plate, whereas for batteries intended to provide more capacity over longer periods of time at lower discharge rates, usually thicker plates are then used. This becomes a trade-off between the available material that the acid can easily migrate or diffuse into, and providing a thicker, more rigid support for the plate to last longer in application.
Analysis of the active material inside a battery has always been challenging due to its destructive nature. The battery has to be cut open and the plates disassembled; that can then only provide a snapshot in time of what the battery's state or condition is. This usually relates to the scientists wanting to know the battery's state of charge (SoC) and state of health (SoH). In a battery, the most important and probably the only chemical parameters one can comfortably measure as an analyst are the chemical properties that include its elemental and phase composition. These techniques usually rely on atomic absorption or X-ray fluorescence-type techniques, as well as advanced methods such as scanning electron microscopy and powder X-ray diffraction. There are also electrochemical analytical techniques that can be applied, including impedance spectroscopy and cyclic voltammetry, among others.
On the other hand, physicochemical properties include the strength of the plates, the available surface area, and the porosity of the active material. Surface area analysis is typically done by nitrogen adsorption techniques, and in this study, the porosity of the plates used in the lead-acid battery was measured. Porosity relates to the available free space that is within the active material for the acid to move freely into and to be in contact with the active sites that will then allow for an electrochemical reaction to take place. If the porosity is too high, there will be limited connective pathways between the various active material particles, increasing the likelihood of disconnection. If the porosity is too low, less of the acid will be able to reach the active sites, thereby reducing the available capacity.
Traditionally, the porosity of solid materials that have micro- to meso-sized pores is measured by mercury porosimetry. This required the active material to be physically removed from the plate in order to fit into the instrument's sample holder. This has a number of disadvantages, namely, only a representative sample from a plate area is taken; the sample as such is disconnected from the grid or current collector, thereby inducing additional cracks and cavities in the material; and many laboratories have moved away from the use of mercury due to its toxicity. The advantage of the technique is its ability to provide an estimate of the pore size distribution of the material within a certain range.
This study proposes a technique that makes use of the entire plate in measuring the total porosity of the active material by using Archimedes' principle. In its context of determining material density, Archimedes' principle states that the buoyant force on an object that is immersed in a fluid is equal to the weight of the fluid displaced by that object. This principle allows one to calculate an object's density by measuring its weight in air and its weight when submerged in a known fluid. This buoyant force is then used to calculate the volume of the displaced fluid, which is equal to the volume of the object.
The technique can be easily set up in a laboratory to measure the porosity of lead-acid battery plates that have been subjected to certain manufacturing or testing conditions. Even though the technique is still destructive in the sense of having to cut the battery open to remove the plates for analysis, the porosity of the entire plate is considered. Hence, the method measures the average porosity over the entire plate, capturing variations of certain regions of the plate that are usually not taken into account. These variations typically occur when working with relatively large plates, where possible manufacturing inconsistencies and the effects of acid stratification can affect specific plate regions over time. However, a limitation of the glycerol displacement method is that it measures porosity based on permeable pores. This means that it is possible to underestimate the plate's porosity if glycerol does not fully penetrate the pores of the active mass. When closed pores are present, the technique indirectly correlates with what happens inside the battery during application, since the acid would also not be able to completely penetrate areas of the active mass that have closed pores. Despite this limitation, the method remains safe and cost-effective and is suitable for measuring the porosity of battery plates.
In this study, the porosities of both the negative and positive plates of a relatively small 7.2 Ah valve-regulated lead-acid (VRLA) battery are measured. These batteries are typically used in household alarm and gate motor control systems. The effect on the batteries' plate porosity and chemical phase composition was studied in terms of the possible aging mechanism to which the battery was exposed. One being excessive calendar aging or shelf life, and the other being repeated capacity cycling without sufficient recharging. These are typical conditions that such batteries are exposed to. Those that remain on the electrical wholesaler's shelves for many months and sometimes years without receiving a boost charge. Moreover, those batteries that are used in standby power supply systems are subjected to repeated "load-shedding-type" capacity cycling, where the inverter system's recharge is insufficient to provide the necessary energy to fully recharge the battery during the short recharge periods available.