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The above equation is universally accepted as standard for computing friction factor of rough pipes and incorporated in most thermohydraulic simulation softwares available at the market. Moody (1944) concluded that the Colebrook (1939) equation was adequate for friction factor calculations for any Reynolds nuer greater than 2000.

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Thermohydraulic performance parameter (TPP) is also evaluated depending on the friction factor (f) and Nusselt nuer (Nu) values for SAH. The maximum Thermohydraulic performance parameter (TPP) is observed at Reynolds nuer of 15000 in case of

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