Copper-ion solid-state battery systems involving sulphonium iodide electrolytes
THE past 10 years has seen a considerable interest in solid-state battery systems involving electrolytes based on silver iodide1–3. Studies of electrolytes involving organic sulphonium iodides in conjunction with silver iodide have been reported3,5–9, but recently the possibility of using cuprous ions to replace silver ions as the mobile species has attracted attention, because of the potential advantage of lower cost and higher voltage. We report here the results of our investigations of sulphonium iodide–cuprous iodide electrolytes.
Changes in electrolyte structure in solid state cells during discharge: Extended x-ray absorption fine structure study
Abstract The first EXAFS study of a solid state battery system is reported. The working cell is based on a copper(I) iodide-sulphonium iodide electrolyte. The EXAFS results clearly indicate that cell modification occurs during cell discharge.
Effect of superficial gas velocity on the particle temperature distribution in a fluidized bed with heat production
The heat transfer behavior of particles and gas in an olefin polymerization fluidized bed was numerically analyzed using an in-house developed 3-D computational fluid dynamics discrete element model (CFD-DEM). First the implementation of the model was verified by comparing simulation results with analytical results. A constant volumetric heat production rate was implemented in the particle energy equation to mimic the heat production due to the polymerization reaction. It was found that the probability density function (PDF) of the particle temperature becomes more homogeneous with increasing superficial gas velocity. Furthermore, instantaneous snapshots of the thermal driving force (the difference between the single particle temperature and bed-average gas temperature, Tp− ) for different heat production rates provide detailed insight in the particle temperature distribution inside the fluidized bed. The time- and bed-averaged particle convective heat transfer coefficient, which was calculated by Gunn׳s correlation, was found to be independent of the superficial gas velocity. This is explained by the fact that the relative velocity of gas and particles in the emulsion phase, where most of the particles and gas interact, is hardly influenced when increasing the gas superficial velocity. From the spatial distribution of Nusselt number, it becomes apparent that the high heat transfer regions are found in the wake of rising bubbles, whereas low heat transfer rates are found in the clouds of the bubbles.