Heat Transfer
Dietus-Boelter equation cannot be used for molten metals mainly due to its very low

Prandtl number
Grashoff number
viscosity
thermal conductivity

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Heat Transfer
A process stream of dilute aqueous solution flowing at the rate of10 Kg.s⁻¹ is to be heated. Steam condensate at 95°C is available for heating purpose, also at a rate of 10 Kg.s⁻¹. A 1 - 1 shell and tube heat exchanger is available. The best arrangement is

Parallel flow with process stream on shell side
Parallel flow with process stream on tube side
Counter flow with process stream on tube side
Counter flow with process stream on shell side

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Heat Transfer
Nusselt number is the ratio of the

None of these
Heat flux at the wall to that across the entire pipe
Temperature gradient of the wall to that across the entire pipe
Temperature difference to the temperature gradient at the wall

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