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

Grashoff number
Prandtl number
viscosity
thermal conductivity

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Heat Transfer
Condensing film co-efficient for steam on horizontal tubes ranges from 5000 to 15000 Kcal/hr.m² .°C. Condensation of vapor is carried out inside the tube in a shell and tube heat exchanger, when the

Higher condensing film co-efficient is desired
Temperature of the incoming vapor is very high
Lower pressure drop through the exchanger is desired
Condensate is corrosive in nature

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