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______________?
A. Nu = 0.023 Re0.8. Pr0.4
B. Nu = (π/2) Gz
C. Nu = (2/π) Gz
D. Nu = 2Gz0.5
A. Nu = 0.023 Re0.8. Pr0.4
B. Nu = (π/2) Gz
C. Nu = (2/π) Gz
D. Nu = 2Gz0.5
A. Heat flux
B. Nusselt number
C. Prandtl number
D. Schmidt number
A. Increasing temperature of the vapour
B. Decreasing temperature of the vapour
C. Increasing viscosity of the film of condensate
D. Increasing temperature drop
A. Increases
B. Decreases
C. Remain same
D. First increases upto a certain temperature and then becomes constant
With increase in temperature, the thermal conductivity of most liquids_________________? Read More »
Chemical Heat Transfer A. Once
B. Twice
C. Thrice
D. Four times
A. Concentration
B. Viscosity
C. Super-saturation
D. Density
A. Current
B. Voltage
C. Resistance
D. None of these
Heat flux, as defined in heat flow is analogous to _______________ in electricity flow? Read More »
Chemical Heat Transfer A. x/KA
B. KA/x
C. K/Ax
D. A/Kx
A. Multipass heat exchanger
B. Baffled heat exchanger
C. Condensation of mixed vapour in a condenser
D. All A. B. and C.
LMTD can’t be used as such without a correction factor for the_________________? Read More »
Chemical Heat Transfer A. Vacuum
B. High pressure
C. High residence time
D. None of these
Heat sensitive materials can be concentrated in an evaporator employing_______________? Read More »
Chemical Heat Transfer