1 |
Derive general heat conduction equation in
rectangular coordinate system |
2 |
Derive general heat conduction equation in cylindrical
coordinate system |
3 |
Explain
thermal Contact resistance. How contact pressure effects thermal contact
resistance? |
4 |
For cylinder, prove that critical radius of
insulation, r critical = k/h, where k=thermal conductivity of insulation and
h=convective heat transfer coefficient. Explain effect of thickness of
insulation on heat transfer. |
5 |
Define : (1) Emissivity (2) Monochromatic
emissive power (3) Opaque body (4) Radiosity (5) Radiation intensity (6)
Solid angle |
6 |
For natural convection heat transfer, prove
that Nu=φ(Pr)(Gr), where Nu=Nusselt number, Pr=Prandlt number and Gr=Grashoff
number. |
7 |
Derive an equation for heat transfer from
very thin and long enough fin so that the heat loss from the fin tip may be
assumed negligible. |
8 |
What is physical significance of
dimensionless parameters? Explain in brief |
9 |
Derive equation of NTU for parallel flow
heat exchanger |
10 |
Derive equation of LMTD for parallel flow
heat exchanger. |
11 |
Derive equation of logarithmic mean
temperature difference for parallel flow Heat-exchanger. |
12 |
Prove that intensity of normal radiation is
1/π times the emissive power. 0 |
13 |
Write general heat conduction equation for
non-homogeneous material, self heat generating and unsteady three-dimensional
heat flow in cylindrical coordinates. Name and state the unit of each
variable. Step 1. Reduces above equation to one dimensional Step 2. Reduces
step 1 equation for steady and without heat generation Step 3. Reduces step 2
equation for homogeneous and isotropic material Step 4. Reduces step 3
equation to r(dt/dr) = constant. |
14 |
By dimensional analysis show that for
natural convection heat transfer the Nusselt number can be expressed as a
function of Grashof number and Prandtl number. |
15 |
Derive the relation for temperature
variation with respect to time, instantaneous heat transfer rate and total
heat transfer using lumped parameter analysis. |
16 |
Derive general heat conduction equation in
cylindrical coordinate system. |
17 |
Derive an expression for heat transfer for
an adequately long of Rectangular fin with insulated tip. |
18 |
Explain term Boiling also explain various
regimes of boiling |
19 |
State the relationship between Nusselt,
Grashoff and Prandtl number in case of heat transfer by nature convection from a
vertical plate |
20 |
In a counter flow heat double pipe heat
exchanger ,water is heated from 250C to 650C by oil with specific heat of
1.45 kJ/kg K and mass flow rate of 0.9 kf/s. The oil is cooled from 2300C to
1600C. If overall Heat transfer coefficient is 420 W/m2 0C. calculate
following (i) The rate of heat transfer (ii) The mass flow rate of water ,
and (iii) The surface area of heat exchanger |
21 |
A solid sphere of 1 cm made up of steel is
at initially at 3000Ctemperature. Properties of steel : k =60 WmK Density =
7800 kg/m 3 , sp. Heat =434J/kg K Calculate the time required for cooling it
up to 500Cin the following two cases (i) cooling medium is air at 250Cwith h
= 20 W/m2 K (ii) cooling medium is water at 250C with h =100 W/m2K |
22 |
A pipe carrying the liquid at -20o C is
10mm in outer diameter and is exposed to ambient at 25o C with convective
heat transfer coefficient of 50W/m2 K. It is proposed to apply the insulation
of material having thermal conductivity of 0.5W/mK. Determine the thickness
of insulation beyond which the heat gain will be reduced. Also calculate the
heat loss for 2.5mm, 7.5mm and 15mm thickness of insulation over 1m length.
Which one is more effective thickness of insulation? |
23 |
Two rods A and B of equal diameter and
equal length, but of different materials are used as fins. The both rods are
attached to a plain wall maintained at 160o C, while they are exposed to air
at 30o C. The end temperature of rod A is 100o C and that of the rod B is 80o
C. If the thermal conductivity of rod A is 380 W/mK, calculate the thermal
conductivity of rod B. This fin can be assumed as short with end insulated. |
24 |
A steel tube of 5 cm inner diameter and 8
cm outer diameter (k = 16 W/mK), is covered with an insulation of 3 cm
thickness (k = 0.3 W/mK). A hot gas at 350o C h = 400 W/m2 K flows. Calculate
the heat loss from the tube for 20 meter length. Also calculate the
temperature at the interface of insulation and steel. |
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