Modelling of boiling in square channels partially filled with porous medium

Investigation of boiling in a square channel, which is filled partly with porous medium, is reported. Influence of major parameters such as porosity and extent of filling of the porous medium on heat transfer rate, vapour volume fraction, vapour generation rate and pressure drop are analyzed. A new solver utilizing the framework of open-source CFD code OpenFOAM is developed to investigate the problem. It is found that addition of porous medium increases fluid temperature, vapour volume fraction, heat transfer and vapour generation rate. It is also established that heat transfer increases on lowering the porosity of porous matrix, when the ratio of thickness of porous medium to channel height (Hp*) is greater than 0.4. In addition, heat transfer rate increases if the porosity increases for Hp* < 0.4, but not significantly, as compared to the cases with Hp* > 0.4. Moreover, there is an increase in pressure drop for an increase in thickness and a decrease in the porosity. It is also found that for twophase heat transfer, the maximum Nusselt number is approximately 4.8 times higher than that for the singlephase heat transfer in the same channel.

Automated summary

This study reports on the investigation of boiling in a square channel with partial filling of porous medium and analyzes the influence of parameters such as porosity and extent of filling on heat transfer and pressure drop. A new solver based on OpenFOAM is developed to study the problem. The results show that adding porous medium increases fluid temperature, heat transfer, and vapor generation rate. Heat transfer also increases with decreasing porosity for a certain ratio of porous medium thickness to channel height. However, the increase in heat transfer is not significant when the ratio is below a certain value. Furthermore, an increase in thickness and a decrease in porosity lead to an increase in pressure drop. Additionally, the maximum Nusselt number for two-phase heat transfer is approximately 4.8 times higher than that for single-phase heat transfer in the same channel.