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Chemical Heat Transfer

The thermal boundary layer at NPr > 1 ?

The thermal boundary layer at NPr > 1 ? A. Is thicker than hydrodynamic boundary layerB. Is thinner than hydrodynamic boundary layer C. And the hydrodynamic boundary layers are identical D. Disappears

The overall heat transfer co-efficient for a shell and tube heat exchanger for clean surfaces is U0 = 400 W/m2.K. The fouling factor after one year of operation is found to be hd0 = 2000 W/m2.K. The overall heat transfer co-efficient at this time is _____________________?

The overall heat transfer co-efficient for a shell and tube heat exchanger for clean surfaces is U0 = 400 W/m2.K. The fouling factor after one year of operation is found to be hd0 = 2000 W/m2.K. The overall heat transfer co-efficient at this time is _____________________? A. 1200 W/m2.K B. 894 W/m2.KC. 333 W/m2.K D….