Parallel flow type
Counter flow type
Cross flow type
Regenerator type
C. Cross flow type
Convection
Radiation
Conduction
Both convection and conduction
Thermal resistance
Thermal coefficient
Temperature gradient
Thermal conductivity
Conduction
Convection
Radiation
Conduction and convection
Density
Coefficient of viscosity
Gravitational force
All of these
1 : 1
2 : 1
1 : 2
4 : 1
Equal to one
Greater than one
Less than one
Equal to Nusselt number
Q = [2πlk (T₁ - T₂)]/2.3 log (r₂/r₁)
Q = 2.3 log (r₂/r₁)/[2πlk (T₁ - T₂)]
Q = [2π (T₁ - T₂)]/2.3 lk log (r₂/r₁)
Q = = 2πlk/2.3 (T₁ - T₂) log (r₂/r₁)
Watt/mK
Watt/m²K²
Watt/m²K4
Watt/mK²
Their atoms collide frequently
Their atoms are relatively far apart
They contain free electrons
They have high density
Moisture
Density
Temperature
All of the above
Increases
Decreases
Remain constant
May increase or decrease depending on temperature
-1/3
-2/3
1
-1
Higher
Lower
Same
Depends on the area of heat exchanger
Minimum energy
Maximum energy
Both (A) and (B)
None of these
W/m²K
W/m²
W/mK
W/m
Melting of ice
Boiler furnaces
Condensation of steam in condenser
None of these
m²/hr
m²/hr °C
kcal/m² hr
kcal/m. hr °C
From one particle of the body to another without the actual motion of the particles
From one particle of the body to another by the actual motion of the heated particles
From a hot body to a cold body, in a straight line, without affecting the intervening medium
None of the above
Liquids
Energy
Temperature
Entropy
Radiators in automobile
Condensers and boilers in steam plants
Condensers and evaporators in refrigeration and air conditioning units
All of the above
Directly proportional to the surface area
Directly proportional to the difference of temperatures between the two bodies
Either (A) or (B)
Both (A) and (B)
Absolute temperature (T)
I²
F
T
Grey body
Brilliant white polished body
Red hot body
Black body
Hr (time)
Sq. m (area)
°C (temperature)
K.cal (heat)
25 mm
40 mm
160 mm
800 mm
Reflected
Refracted
Transmitted
Absorbed
Improve heat transfer
Provide support for tubes
Prevent stagnation of shell side fluid
All of these
Thermometer
Thermistor
Thermocouple
None of these
The total radiation from a black body per second per unit area is directly proportional to the fourth power of the absolute temperature
The wave length corresponding to the maximum energy is proportional to the absolute temperature
The ratio of the emissive power and absorptive power of all bodies is the same and is equal to the emissive power of a perfectly black body
None of the above
Direct mixing of hot and cold fluids
A complete separation between hot and cold fluids
Flow of hot and cold fluids alternately over a surface
Generation of heat again and again