STEADY STATE OF HEAT FLOW
Let us take a bar of uniform
cross-section and heat it at one end. Each cross-section of the bar receives
heat by conduction from the adjacent cross-section towards the heated end.
This heat is spent in three ways; a part
is absorbed by the cross-section to increase its temperature, another part
escapes out from the sides of the cross-section, and the third is conducted to
the next cross-section. The same happens at the next cross-section, and so on.
Thus the temperature of each part of the
bar rises, and the bar is said to be in a "variable state".
After some time, however, a state is reached when temperature at each
point of the bar becomes stationary. This is called the 'steady state'.
In this state no heat is absorbed by the
bar. The heat that reaches any section is transferred to the next, except that
some heat may escape out from the sides. (The steady state is not the same as
thermal equilibrium, in which all parts of the bar must have the same
temperature).
The steady state is tried to be achieved
in an experiment in which the heat supplied to a body in a given time is to be
measured, such as Searle's experiment for determining the thermal conductivity
of a rod.
In this experiment the heat supplied at
one end of the rod is determined by measuring the rise in temperature of a
known amount of water flowing around the other end.
The measurement is done after the steady
state is reached because it is only then that all the heat supplied at one end
reaches the other end where it is taken in by water.
Before the steady state, a part of the
heat supplied is used up in increasing the temperature of the rod and hence the
heat taken in by water is not equal to the heat supplied to the rod.
THERMAL
CONDUCTIVITY
The ability of a substance to conduct
heat energy is measured by its thermal conductivity.
Expression
for Thermal Conductivity
Consider a slab of material of length x
metre (thickness) and area of cross-section A as shown in fig. 1.5.
One end of the slab is maintained at a
higher temperature e1 (hot end) and the other end at a lower temperature 02
(cold end). Now, heat flows from hot end to cold end.
It is found that the amount of heat (Q)
conducted from one end to the other end is
• directly proportional to area of cross-section
(A). n (A). I
• directly proportional to temperature
difference between the ends (θ1 – θ2).
• directly proportional to time of
conduction (t).
• inversely proportional to length (x)
between the faces (Shaded in fig. 1.5)
Combining all these factors, we have
where K is a proportionality constant.
It is known as coefficient of thermal conductivity or simply thermal
conductivity. Its value depends on the nature of material.
K = Q x / A (θ1-θ2) t θ1 - θ2 = 1kelvin
x = 1 metre t = 1 second
Then,
K = Q
This condition defines othe coefficient
of thermal conductivity.
Definition
It is defined as the amount of heat
conducted per second normally across unit area of cross-section of the material
per unit temperature difference per unit length.
The quantity
θ1 – θ2 / x denotes the rate of fall temperature
with respect to distance. It is known as
temperature gradient.
For the smaller values, θ1 –
θ2 / x is written as dθ / dx
Rewriting the expression (2), we have is
Q = - KA dθ / dx t ...(3)
To indicate dθ / dx is negative, a negative sign is included in the
R.H.S of the equation, since it signifies that the temperature decreases with
distance.
Unit:
We know that K =
Substituting the corresponding units, we
have
= joule x metre / metre2 x kelvin x second
= joule / second x metre x kelvin
= watt / metre x kelvin W /m / K
= Wm-1 K-1
Therefore, the unit of thermal
conductivity is Wm-1 K-1
Note
Thermal conductivity denotes the heat heat conducting
characteristics of the substances. Generally metals are good conductors of heat
(e.g., silver, copper) and non-metals are bad conductors of heat (Air, glass,
wood).
Thermal conductivities of some common
materials are given in the table. 1.1.
The knowledge about thermal conductivity
of the material is very much essential in selecting the materials for suitable
engineering applications (design and construction).
ANNA UNIVERSITY SOLVED PROBLEMS
Problem
1.1
A rod 0.25 m long and 0.892 x 10-4
m2 area of cross section is heated at one end through 393 K while
the other end is kept at 323 K. The quantity of heat which will flow in 15
minutes along the rod is 8.811 x 10 joule. Calculate thermal conductivity of
the rod. (A.U Dec 2020)
Given
data
Area of cross section of the rod (A) =
0.892 × 10-4 m2
Distance between two ends of the rod (x)
= 0.25 m
Temperature difference ( θ1 –
θ2 ) = 393 K - 323 K = 70 K
Quantity of heat conducted (Q) = 8.811 ×
103 joule
Time of flow of heat (t) = 15 minutes = 15
x 60 = 900 second
Solution
We know that K = Q x / A (θ1 – θ2) t
Substituting the given values, we have
K
= 8.811 × 103 × 0.25 / 0.892 x 10-4 x 70 x 900
Thermal
conductivity K = 392 Wm -1K-1
Problem
1.2
How much heat will be conducted through
a slab of area 90 x 10-4 m2 and
thickness 1.2 × 10-3 m in one one second when its opposite faces are
maintained at difference in temperature of 20 K. The The coefficient of thermal
conductivity of that material is 0.04 Wm-1 K-1
Given
data
Area of the slab A = 90 x 10-4
m2
Thickness of the slab x = 1.2 x 10-3
m
Temperature difference (θ1 –
θ2) = 20 K
Thermal conductivity K = 0.04 Wm -1
K-1
Time taken t = 1 second
Solution:
Amount of heat conducted
Q = KA (θ1 – θ2) t
/ x
Substituting the given values, we have
Q = 0.04 × 90 × 10-4 × 20 ×
1 / 1.2 x 10-3
Q = 6 joule
Amount
of heat conducted in one second = 6 joule.
Problem
1.3
The total area of the glass window is
0.5 m2. Calculate how much heat is conducted per hour through the
glass window if thickness of the glass is 7 × 10 me the temperature of the
inside surface is 25°C and of the outside surface is 40°C. Thermal conductivity
of glass is 1.0 Wm- 1K-1
[A.U jan 2020]
Given
data
Area of glass window A = 0.5 m2
Thickness of the glass x = 7 x 10-3
m
θ1
= 40°C = 273 + 40 = 313 K
θ2 = 25°C 273 + 25 = 298 K
Thermal conductivity K = 1 Wm-1
K-1
t = 1 hour = 60 x 60 second
= 3600 second
Solution
Amount of heat conducted
Q = KA (θ1 – θ2) t
/ x
Q =
1 x 0.5 × (313 - 298) × 3600 / 7 x 10-3
Q
= 27000 / 7 × 10-3
Q = 3857 × 103 J
Q = 3.857 × 106 J