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The study evaluates the heat transfer and pressure drop performance of a tube-in-tube heat exchanger using Bakelite helical screw tape and aluminum hemispherical cup shape inserts under turbulent flow conditions. Experimental results show significant enhancements in heat transfer, with Nusselt number ratios for helical screw tape ranging from 2.51 to 2.7 and friction factor ratios from 4.12 to 4.13, while cup shape inserts exhibited Nusselt number ratios between 1.38 and 1.62. The findings suggest that vary

Author

AlaaAli

Language

EN