A. Boiling
B. Nusselt
C. Burnout
A. Laminar
B. Transition
C. Both A & B
A. Not related with
C. Equal to
D. Greater than
A. Thermal conductivity
C. Heat capacity
D. Viscosity
A. Long tube vertical evaporator
C. Agitated film evaporator
D. None of these
B. None of these
C. When fluid flows past a smooth surface
D. At low velocity
B. Temperature of the feed
C. Rate of heat transfer
D. Ratio of the weight of the thin liquor to thick liquor
A. (COP)R = (COP)HP = 0.6
B. (COP)R = (COP)HP = 2.5
C. (COP)R = 2.5; (COP)HP = 1.5
A. First decreases upto certain temperature and then increases
B. Decreases
D. Remain constant
A. Nature of heating surface and distribution of bubbles
B. Viscosity of water
D. Surface tension of water
A. ?x + ?y
B. 1/?x + 1/?y
C. ?x . ?y
B. W/m
C. W/m.k
D. None, a is just a number
A. None of these
C. Wavelength of radiation
D. Nature of the body
A. Is not affected
B. May increase or decrease; depends on the feed
D. Increases
B. St = 4f
C. St = f/4
D. St = f1/2
A. Heat flows in one direction only
C. Temperature distribution is independent of time
D. Three dimensional heat flow is concerned
A. Avoid cavitation
C. None of these
D. Avoid frequent priming
B. Conduction
C. Forced convection
A. Feed is introduced in the first effect
B. No pumps are required between successive effects
A. High viscosity liquid is to be cooled
B. A corrosive liquid is to be heated
D. Overall heat transfer co-efficient is very high
A. Same velocity profile or equal eddy diffusivities
B. Thermal or pressure mass diffusion
C. Viscous heating or chemical reaction
A. 100-500
C. Oct-50
D. 1000-1500
C. Superheat the steam
D. Remove condensate from the steam pipelines
A. May increase or decrease, depends on the type of baffle
C. Does not affect
D. Decreases
B. 1/CE
C. CE
D. E/C
A. Grashoff
C. Stanton
D. Condensation
A. Corrosive nature
B. Thermal conductivity
D. Density
A. Dependent on metal resistance
B. Always higher than h2
D. Always less than h1
A. Fouling characteristic
B. Corrosiveness
C. Viscosity
A. 20.8
B. 40.4
C. 20.4
A. Remains unchanged
C. Increases exponentially
A. 0.05
B. 0.15
C. 0.5
A. Kistyakowsky
C. Lees
D. Antoine
A. All will cool at the same rate
B. Plate
C. Cube
B. May increase or decrease; depends on the gas
C. Decreases
D. Remains unchanged
A. r = h/k
B. r = 2k/h
C. r = k/2h
A. 50 -100 W/m2.K
B. 1000 1500 BTU/hr. ft.2F
C. 50 -100 Kcal/hr.m2.C
A. Peclet number
B. Stanton number
C. Brinkman number
B. 26
C. 18
D. 1
C. Backward feed
D. High pressure
A. Forced convection
C. Conduction
D. Natural convection
A. Remain unchanged
C. Increase by 1.8 times
D. Decrease by 22
B. 0.001 to 1
C. 0.5 to 5
D. 120 to 400
A. Condenser
B. Heat exchanger
C. Multiple effect evaporator
B. High evaporation rate
C. High vacuum in the evaporator
D. High heat transfer rate
A. Carbon black
C. Tar
D. Steel
A. W/m2K
B. m2K
C. mK/W
A. Temperature
B. Porosity
D. Neither A. nor B.
B. Loosing latent heat
C. Vaporisation due to heat loss to air
D. Heat transfer to surroundings
B. 1
C. > 1
D. Between 1 & 2
Showing 4151 to 4200 of 8709 mcqs