A BTU/hr.ft.2 °F is equal to 4.88 kcal/hr. m.2°C 1 kcal/hr. m²°C 1 kcal/hr. m².°K None of these TRUE ANSWER : ? YOUR ANSWER : ?
Which characteristic of a fluid is not important in deciding its route in a shell and tube heat exchanger? Corrosiveness Fouling characteristic None of these Viscosity TRUE ANSWER : ? YOUR ANSWER : ?
For a liquid in laminar flow through a very long tube, when the exit fluid temperature approaches the wall temperature, the equation to be used is Nu = 0.023 Re0.8 . Pr0.4 Nu = Gz Nu = Gz Nu = 2Gz0.5 TRUE ANSWER : ? YOUR ANSWER : ?
A metal wire of 0.01 m dia and thermal conductivity 200 W/m.K is exposed to a fluid stream with a convective heat transfer coefficient of 100 W/m².K. The Biot number is 0.0035 5.6 0.025 3.5 TRUE ANSWER : ? YOUR ANSWER : ?
The rate of heat transfer is a product of overall heat transfer co-efficient, the difference in temperature and the Heating volume Heat transfer area Nusselt number None of these TRUE ANSWER : ? YOUR ANSWER : ?
If Prandtl number is greater than the Schmidt number, then the none of the listed here thermal & concentration boundary layers are of equal thickness thermal boundary layer lies inside the concentration boundary layer concentration boundary layer lies inside the thermal boundary layer TRUE ANSWER : ? YOUR ANSWER : ?
The ratio of momentum diffusivity to thermal diffusivity is the __________ number. Nusselt Grashoff Prandtl Stanton TRUE ANSWER : ? YOUR ANSWER : ?
The ratio of the total emissive power to the absorptivity for all bodies is same at ther-mal equilibrium. This is __________ law. Planck's Wien's displacement Kirchoffs Stefan-Boltzman TRUE ANSWER : ? YOUR ANSWER : ?
In forced convection, the Nusselt number is a function of Re and Pr Re and Sc Pr and Gr Re and Gr TRUE ANSWER : ? YOUR ANSWER : ?