The thermal conductivity of phase change material (PCM) is one of the essential variables for the fast heat transfer process for latent heat energy storage (LHES) units. The thermal characteristics of a novel LHES rectangular enclosure based on multiple chambers separated by insulating and rigid walls are numerically investigated. The enthalpy‐porosity strategy supported by the finite volume method is implemented to perform the simulation. Simulation results exhibited that thermal charging and discharging performance was enhanced without affecting the system's total heat storage capacity by creating multiple chambers. Liquid fraction, mean temperature, heat flux, contours of liquid fraction and temperature of PCM are demonstrated as a function of the melting time. The thermal charging time of PCM is diminished by increasing the number of chambers. Although, the consequences of the number of chambers on the melting time of PCM are diminished by surging the number of chambers. It was also found that continuously raising the heating temperature is not beneficial for reducing the total time of liquid fraction during melting. Thermal discharging performance is poor than that of the thermal charging process.

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The flow and heat transfer characteristics of Oberbeck convection of a chiral fluid in the presence of the transverse magnetic field, viscous dissipation and variable viscosity are investigated. The coupled non-linear ordinary differential equations governing the flow and heat transfer characteristics of the problem are solved both analytically and numerically. The analytical solutions are obtained using a regular perturbation and numerical solutions obtained using finite difference method. The solution is valid for small values of Buoyancy parameter N and variable viscosity parameter R 1 . The analytical results are compared with the numerical results and found good agreement. The role of temperature dependent viscosity and viscous dissipation on velocity, temperature, skin friction and the rate of heat transfer are determined. The results are depicted graphically, from these graphs it is noticed that the velocity is parabolic in nature and increases with an increase in magnetochiral number M . Physically this is attributed to the fact that magnetochiral number introduces small scale turbulences. NOMENCLATURE 0 R viscosity variation parameter Re Reynolds number T absolute temperature 1  coefficient of thermal expansion of viscosity 2  coefficient of thermal expansion of density  dielectric constant  chirality coefficient  kinematic viscosity f  viscosity of fluid  magnetic permeability  viscous dissipation  density of fluid e  distribution of electric charge density  transportive properties  non dimensional temperature 0 reference quantity

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