Heat Conduction Through Hollow Spheres in Dairy Engineering

 
Dr. J. Badshah
University Professor – cum - Chief Scientist
Dairy Engineering Department
Sanjay Gandhi Institute of Dairy Technology,
Jagdeopath, Patna
(Bihar Animal Sciences University, Patna)
 
Conduction Through Hollow Spheres
 
Let us consider a Hollow sphere of inner radius r
1
  and outer
radius r
2
  and made up of materials having constant thermal
conductivity. The inner hot fluid temperature as t
1
 and outer
surface temperature as t
2
 with the condition that t
1
>t
2 
 .
Therefore temperature varies only radially and we can
assume that this radial direction is x-direction. Thus
temperature field is one dimensional and the isothermal
surfaces are spherical surfaces possessing a common axis
with the sphere.
Consider a small element of thickness dr at any radius r. Area
of element through which heat is transmitted, A = 4 πr
2
 
 
Conduction Through Hollow Shere
 
 
During steady state, the rate of heat transfer is given by
Q = -K. 4πr
2 
 . dt/dr
Rearranging and integrating the above  equation, we obtain for
limit from r
1
 to r
2
 with respect to time from t
1 
to t
2
:
Q ∫dr/r
2 
 = - 4πK ∫dt
- Q [1/r
2
 – 1/ r
1
] = -4πk (t
2 
 - t
1
)
Q = (t
1
 – t
2
) /[(r
2
 – r
1
)/4πKr
1
r
2
 ]
Case II: Variable thermal conductivity, we have:
Q = [
4πK
0
r
1
r
2
 / (r
2
 – r
1
)][1 
β
/2 (
t
1 
 + t
2 
 )](t
1
 – t
2
)
Observe Figure of steady state conduction through Hollow
sphere on group whatsapp.
 
Logarithmic Mean Area For Hollow Sphere
 
It is considered that the heat flow from the hollow sphere is of the sme
form as that of the plane wall. Expression for heat flow through the
hollow sphere and plane wall are :
 Q sphere = (t
1
 – t
2
) /[(r
2
 – r
1
)/4πKr
1
r
2
 ]
Q plane wall = (t
1
 – t
2
) /[(r
2
 – r
1
)/K A
m
]
Log mean Area , A
m 
 is so chosen that the heat flow through the sphere
and plane wall will be equal for the same thermal potential.
Q sphere = Q plane wall
(t
1
 – t
2
) /[(r
2
 – r
1
)/4πKr
1
r
2
 ] = (t
1
 – t
2
) /[(r
2
 – r
1
)/K A
m
]
Therefore, A
m
 = 4πr
1
r
2
(A
m
)
2 
 = (4πr
1
r
2
)
2
 = (4πr
1
)
2
 x (4πr
2
 )
2
(A
m
)
2 
 = A
i
 x A
o
A
m
 = √ A
i
 x A
o
 = 4π(r
m
 )
2 
 = 4πr
1
r
2
Therefore Logmean radius   r
m
= √(r
1
r
2
)
 
 
Numericals on conduction through sphere
 
A spherical shaped vessel of 1.4 m diameter is 90 mm thick.
Find the rate of heat leakage, if the temperature difference
between the inner and outer surfaces is 220°C. Thermal
conductivity of the material of the sphere is 0.083 W/m°C.
Solution : Use The formula:
Q sphere = (t
1
 – t
2
) /[(r
2
 – r
1
)/4πKr
1
r
2
 ]
R2 = 0.7 m
R1 = 0.7 – 0.09 = 0.61 m
Q = 1088.67 W
 
 
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Dr. J. Badshah, a University Professor cum Chief Scientist at Sanjay Gandhi Institute of Dairy Technology, explains the conduction through hollow spheres with varying thermal conductivity. The concept of logarithmic mean area for hollow spheres and solving numericals related to conduction through a spherical vessel are discussed in detail.

  • Heat Conduction
  • Dairy Engineering
  • Hollow Spheres
  • Thermal Conductivity
  • Numericals

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  1. Dr. J. Badshah University Professor cum - Chief Scientist Dairy Engineering Department Sanjay Gandhi Institute of Dairy Technology, Jagdeopath, Patna (Bihar Animal Sciences University, Patna)

  2. Conduction Through Hollow Spheres Let us consider a Hollow sphere of inner radius r1and outer radius r2and made up of materials having constant thermal conductivity. The inner hot fluid temperature as t1and outer surface temperatureas t2with thecondition that t1>t2. Therefore temperature varies only radially and we can assume that this radial direction is x-direction. Thus temperature field is one dimensional and the isothermal surfaces are spherical surfaces possessing a common axis with the sphere. Consider a small element of thickness dr at any radius r. Area of element through which heat is transmitted, A = 4 r2

  3. Conduction Through Hollow Shere During steady state, the rate of heat transfer is given by Q = -K. 4 r2 . dt/dr Rearranging and integrating the above equation, we obtain for limit from r1to r2with respect to time from t1 to t2: Q dr/r2 = - 4 K dt - Q [1/r2 1/ r1] = -4 k (t2 - t1) Q = (t1 t2) /[(r2 r1)/4 Kr1r2] Case II: Variable thermal conductivity, we have: Q = [4 K0r1r2/ (r2 r1)][1 /2 (t1 + t2 )](t1 t2) Observe Figure of steady state conduction through Hollow sphere on group whatsapp.

  4. Logarithmic Mean Area For Hollow Sphere It is considered that the heat flow from the hollow sphere is of the sme form as that of the plane wall. Expression for heat flow through the hollow sphereand plane wall are : Q sphere = (t1 t2) /[(r2 r1)/4 Kr1r2] Q plane wall = (t1 t2) /[(r2 r1)/K Am] Log mean Area , Amis so chosen that the heat flow through the sphere and plane wall will be equal forthe same thermal potential. Q sphere = Q plane wall (t1 t2) /[(r2 r1)/4 Kr1r2] = (t1 t2) /[(r2 r1)/K Am] Therefore, Am= 4 r1r2 (Am)2= (4 r1r2)2= (4 r1)2x (4 r2)2 (Am)2= Aix Ao Am= Aix Ao= 4 (rm)2= 4 r1r2 Therefore Logmean radius rm= (r1r2)

  5. Numericals on conduction through sphere A spherical shaped vessel of 1.4 m diameter is 90 mm thick. Find the rate of heat leakage, if the temperature difference between the inner and outer surfaces is 220 C. Thermal conductivity of the material of the sphere is 0.083 W/m C. Solution : Use The formula: Q sphere = (t1 t2) /[(r2 r1)/4 Kr1r2] R2 = 0.7 m R1 = 0.7 0.09 = 0.61 m Q = 1088.67 W

  6. THANK YOU

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