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HEAT CONDUCTION THROUGH A PLANE WALL
β€’ Let us consider a plane wall of homogeneous material through which heat
is flowing in x-direction.
β€’ Let Q +x
L = thickness of the wall T0
A = cross-sectional area of the wall k
k = thermal conductivity of wall material T1
T0 , T1 = temperature maintained at surfaces 1 and 2. 1 2
L
k
β€’ General heat conduction equation is:
πœ•2 𝑇
πœ•π‘₯2
+
πœ•2 𝑇
πœ•π‘¦2
+
πœ•2 𝑇
πœ•π‘§2
+
π‘ž
π‘˜
=
1
𝛼
.
πœ•π‘‡
πœ•π‘‘
β€’ For one dimensional steady state system (
πœ•π‘‡
πœ•π‘‘
= 0)
β€’ With no heat generation (
π‘ž
π‘˜
= 0)
β€’ One dimensional flow (
πœ•2 𝑇
πœ•π‘¦2 =
πœ•2 𝑇
πœ•π‘§2 = 0)
β€’ Then, heat equation will be
πœ•2 𝑇
πœ•π‘₯2 = 0 or
𝑑2 𝑇
𝑑π‘₯2 = 0
𝑑2 𝑇
𝑑π‘₯2
= 0
Integrating the above expression;
𝑑𝑇
𝑑π‘₯
= 𝐢1
Integrating it again;
T = C1.x + C2 ……………….. (1)
Where C1 and C2 are arbitrary constants.
β€’ At x = 0; T = T0
β€’ At x = L; T = T1
β€’ From the expression derived above T = C1.x + C2
β€’ At x = 0;
T0 = C1 (0)+ C2
C2 = T0
β€’ At x = L;
T1 = C1 . L + T0
C1 = (T1 - T0 )/L
Eqn. 1 can be re-written as
T = (
π‘»πŸβˆ’π‘»πŸŽ
𝑳
) . 𝒙 + T0
β€’ Inference:
1. Temperature distribution across the wall is linear.
2. Temperature distribution is independent of k.
From Fourier’s Law, we have
Q = - k. A.
𝑑𝑇
𝑑π‘₯
𝑑
𝑑π‘₯
(
𝑇1βˆ’π‘‡0
𝐿
. π‘₯ + 𝑇0) =
𝑇1βˆ’π‘‡0
𝐿
Fourier’s Law can be re-written as
Q = k. A.(
𝑇0βˆ’π‘‡1
𝐿
)
β€’ Another way of writing the Fourier’s Law is
Q =
𝑇0βˆ’π‘‡1
𝐿/π‘˜π΄
Where L/kA = Thermal Resistance of heat conduction (Rth)cond.
(Rth)cond. = (L/kA)

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Heat conduction through a plane wall

  • 1. HEAT CONDUCTION THROUGH A PLANE WALL β€’ Let us consider a plane wall of homogeneous material through which heat is flowing in x-direction. β€’ Let Q +x L = thickness of the wall T0 A = cross-sectional area of the wall k k = thermal conductivity of wall material T1 T0 , T1 = temperature maintained at surfaces 1 and 2. 1 2 L k
  • 2. β€’ General heat conduction equation is: πœ•2 𝑇 πœ•π‘₯2 + πœ•2 𝑇 πœ•π‘¦2 + πœ•2 𝑇 πœ•π‘§2 + π‘ž π‘˜ = 1 𝛼 . πœ•π‘‡ πœ•π‘‘ β€’ For one dimensional steady state system ( πœ•π‘‡ πœ•π‘‘ = 0) β€’ With no heat generation ( π‘ž π‘˜ = 0) β€’ One dimensional flow ( πœ•2 𝑇 πœ•π‘¦2 = πœ•2 𝑇 πœ•π‘§2 = 0) β€’ Then, heat equation will be πœ•2 𝑇 πœ•π‘₯2 = 0 or 𝑑2 𝑇 𝑑π‘₯2 = 0
  • 3. 𝑑2 𝑇 𝑑π‘₯2 = 0 Integrating the above expression; 𝑑𝑇 𝑑π‘₯ = 𝐢1 Integrating it again; T = C1.x + C2 ……………….. (1) Where C1 and C2 are arbitrary constants.
  • 4. β€’ At x = 0; T = T0 β€’ At x = L; T = T1 β€’ From the expression derived above T = C1.x + C2 β€’ At x = 0; T0 = C1 (0)+ C2 C2 = T0 β€’ At x = L; T1 = C1 . L + T0 C1 = (T1 - T0 )/L Eqn. 1 can be re-written as T = ( π‘»πŸβˆ’π‘»πŸŽ 𝑳 ) . 𝒙 + T0
  • 5. β€’ Inference: 1. Temperature distribution across the wall is linear. 2. Temperature distribution is independent of k. From Fourier’s Law, we have Q = - k. A. 𝑑𝑇 𝑑π‘₯ 𝑑 𝑑π‘₯ ( 𝑇1βˆ’π‘‡0 𝐿 . π‘₯ + 𝑇0) = 𝑇1βˆ’π‘‡0 𝐿 Fourier’s Law can be re-written as Q = k. A.( 𝑇0βˆ’π‘‡1 𝐿 )
  • 6. β€’ Another way of writing the Fourier’s Law is Q = 𝑇0βˆ’π‘‡1 𝐿/π‘˜π΄ Where L/kA = Thermal Resistance of heat conduction (Rth)cond. (Rth)cond. = (L/kA)