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(Ann) #1
812 ENGINEERING THERMODYNAMICS

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\M-therm\Th15-2.pm5

Case II : The heat flow through an insulated wire when critical thickness is used is given
by


Q 2 =^212 0 00343 0 001
012

1
35 0 00343

1
1

ππLt t 1
rr
khr

air Lt t
c
oc

() air
ln ( / )
.

()
ln (. /. )
.

.


+

= − +
×

=^2
18 6

πLt t() 1 air
.

− ...(ii)

∴ Percentage increases in heat flow by using critical thickness of insulation

=
QQ
Q

21
1


× 100 =

1
18.6

1
20.77
1
20.77


× 100 = 11.6%. (Ans.)

15.3. Heat Transfer by Convection


l The rate equation for the convective heat transfer (regardless of particular nature)
between a surface and an adjacent fluid is prescribed by Newton’s law of cooling (Refer
Fig. 15.29)
Q = hA(ts – tf) ...(15.44)
where, Q = Rate of conductive heat transfer,
A = Area exposed to heat transfer,
ts = Surface temperature,
tf = Fluid temperature, and
h = Co-efficient of conductive heat transfer.
The units of h are, h =
Q
At t()s f

W
− mC^2

=
°

or W/m^2 °C or W/m^2 K

The coefficient of convective heat transfer ‘h’ (also known as film heat transfer coefficient)
may be defined as ‘‘the amount of heat transmitted for a unit temperature difference between the
fluid and unit area of surface in unit time.’’
The value of ‘h’ depends on the following factors :
(i) Thermodynamic and transport properties (e.g., viscosity, density, specific heat etc.) ;
(ii) Nature of fluid flow ;
(iii) Geometry of the surface ;
(iv) Prevailing thermal conditions.
Since ‘h’ depends upon several factors, it is difficult to frame a single equation to satisfy all
the variations, however a dimensional analysis gives an equation for the purpose which is given as
under :


h
k

D Z CD

a
= F
HG

I
KJ

ρ
π

c
k

D
L

p
F μ b c
HG

I
KJ

F
HG

I
KJ ...(15.45)

or Nu = Z (Re)a (Pr)b D
L


F c
HG

I
KJ
where, Nu = Nusselt number h
k

F D
HG

I
KJ

,

Re = Reynolds number
ρ
μ

F uD
HG

I
KJ
,
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