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This study investigates the performance of tube-in-tube helically coiled heat exchangers using computational fluid dynamics (CFD) to analyze different configurations of the inner tube. The results indicate that using a hexagonal tube geometry improves the Nusselt Number and friction factor significantly compared to a circular tube, with increases of 17.05% and 15% respectively at a Dean number of 400. The findings contribute to optimizing heat transfer efficiency in various industrial applications.

Author

dabadubada

Language

EN