A. Biot
B. Nusselt
C. Reynolds
D. Prandtl
A. Biot
B. Nusselt
C. Reynolds
D. Prandtl
A. Liquid depth over the heating surface
B. Solution being evaporated
C. Pressure difference between the steam chest and the vapor space above the boiling liquid
D. All A., B. and C.
A. 0.2
B. 0.4
C. 0.6
D. 0.8
A. Heat transfer co-efficient are high
B. There is no risk of contamination
C. There is no mist formation
D. Cost of equipment is lower
A. Dowtherm
B. Molten sodium
C. Water
D. Air
A. Long vertical evaporator
B. Horizontal tube evaporator
C. Agitated film evaporator
D. Calandria vertical tube evaporator
A. Increases
B. Decreases
C. Remain constant
D. May increase or decrease; depends on the material
A. Geometric
B. Arithmetic
C. Logarithmic
D. Either A., B. or C.
A. Re.Gz
B. Nu, Pr
C. Nu, Pr, Re
D. Nu, Gz
A. Heat the water from 0°C to 100°C
B. Evaporate the water
C. To superheat the steam
D. Data insufficient, can’t be predicted