Stacking of microfluidic fuel cells and redox batteries may cause internal current losses and reduced performance compared to single cells. In the present work, these internal current losses are investigated experimentally for an array of two microfluidic vanadium redox batteries based on flow-through porous electrodes. A unique cell array design is proposed, having two pairs of flow-through electrodes situated in a single co-laminar flow manifold. The two electrochemical cells are connected electrically in series and have series fluidic connection through the electrolyte in order to reuse the partially consumed reactants from the first, upstream cell in the second, downstream cell. The cell array prototype demonstrates a maximum power output of 9 mW and a maximum current of 13.5 mA. However, current losses up to 1.75 mA are observed at open circuit, which is attributed to reactant discharge through a parasitic cross-cell comprising of one electrode from each electrochemical cell in the shared manifold. This current loss, appearing in the form of a shunt current, is shown to be proportional to the cell potential. The drop in coulombic efficiency is calculated to quantify the effect of the shunt current. Recommendations for mitigation of shunt current in microfluidic cell arrays are provided. Among these microfluidic electrochemical cells, some have implemented the concept of co-laminar flow rather than a physical membrane to achieve reactant separation. In the former mentioned co-laminar flow cells (CLFCs), wherein species mixing is mainly governed by diffusion, the diffusional interface provides separation between the two flowing streams whilst permitting ion transport. In general, these cells offer great advantages over their conventional counterparts such as the simplicity of the structure, elimination of the membrane and its cost and hydration issues. These membraneless CLFCs thus hold promises of future power generation for portable devices and off-grid sensors.
1,2The first CLFC was introduced by Ferrigno et al. in 2002, using vanadium redox species in a Y-shaped channel.3 Since then, several reviews have been published which summarize the fundamental physics of these devices, 4 and also highlight some of the milestones achieved in device functionality, reactants and architectures, 2,5 for both fuel cells 6-10 and batteries. [11][12][13] The first architectures reported used planar electrodes on the sides or bottom of a micro-channel. 3,7 Jayashree et al. introduced the air breathing cathode architecture that allowed gaseous oxygen transport from the surroundings.14 Kjeang et al. introduced the flow-through electrode architecture that increased both performance characteristics and fuel utilization by utilizing the whole three-dimensional area of a porous carbon electrode.15 Using a derivative cell architecture with dual pass configuration, Lee et al. 11 developed the first microfluidic redox battery (MRB) that was later analyzed by Goulet and Kjeang. 16 This architecture further increased the per...