Heat exchanger

A heat exchanger transfers heat from a hot water stream to a cold one and can be operated in parallel or countercurrent flow as shown below. In what configuration does the heat exchanger work most effectively and transfers the most heat?

  • T h 1 T_{h1} and T c 1 T_{c1} are the input temperatures and T h 2 T_{h2} and T c 2 T_{c2} are the output temperatures of the hot and cold water stream.
  • The water flows have temperature profiles T h ( x ) T_h(x) and T c ( x ) T_c(x) with 0 < x < L 0 <x <L ( L L : length of the heat contact)
  • The heat flow d Q ˙ d\dot Q through a surface area d S = w d x dS = wdx of the heat contact is proportional to the local temperature gradient d Q ˙ = k ( T h ( x ) T c ( x ) ) d S , k : heat conductivity d\dot Q = k (T_h(x) - T_c(x)) dS, \quad k: \text{ heat conductivity}
  • Both water streams have the same volume flow V ˙ = A v \dot V = A v with flow velocity v v and pipe cross section A A
  • A temperature change d T dT of in a volume V V corresponds to a heat transfer d Q = c V d T dQ = c V dT with the specify heat capacity c c .
It depends on the length and thermal conductivity of the pipes Parallel flow Countercurrent flow Both configurations are equal effective

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1 solution

Markus Michelmann
Sep 28, 2017

The local heat transfer rate for both streams read c V ˙ d T h d x d x = d Q ˙ = k w ( T h ( x ) T c ( x ) ) d x ± c V ˙ d T c d x d x = d Q ˙ = k w ( T h ( x ) T c ( x ) ) d x \begin{aligned} c \dot V \frac{dT_h}{dx} dx &= -d\dot Q = -k w (T_h(x) - T_c(x)) dx \\ \pm c \dot V \frac{dT_c}{dx} dx &= d\dot Q = k w (T_h(x) - T_c(x)) dx \\ \end{aligned} where the plus sign and the minus sign in the latter equation respectively denoting the parallel and countercurrent flow. With the parameter λ = 2 k w / c V ˙ \lambda = 2 k w/c \dot V we get the coupled differential equations ( T h ( x ) ± T c ( x ) ) = λ 2 ( 1 1 1 1 ) ( T h ( x ) ± T c ( x ) ) \left( \begin{array}{c} -T_h'(x) \\ \pm T_c'(x) \end{array} \right) = \frac{\lambda}{2} \left( \begin{array}{cc} 1 & - 1\\ 1 & -1 \end{array} \right) \left( \begin{array}{c} T_h(x) \\ \pm T_c(x) \end{array} \right)

Countercurrent Flow

d T h d x = d T c d x \frac{dT_h}{dx} = \frac{dT_c}{dx} applies, so that the gradient T h ( x ) T c ( x ) = Δ T T_h(x) - T_c(x) = \Delta T results a constant. Therefore, the functions show a linear course T h ( x ) = T h 1 a x T c ( x ) = T c 1 + a ( L x ) \begin{aligned} T_h(x) &= T_{h1} - a x \\ T_c(x) &= T_{c1} + a (L - x) \end{aligned} with Δ T = T h 1 T c 1 a L = ( 2 / λ ) T h ( x ) = 2 a / λ \Delta T = T_{h1} - T_{c1} - a L = - (2/\lambda) \cdot T_h'(x) = 2 a/\lambda , so that a = T h 1 T c 1 2 λ + L T c 2 = T c ( 0 ) = T c 1 + L 2 λ + L ( T h 1 T c 1 ) \begin{aligned} a &= \frac{T_{h1} - T_{c1}}{ \frac{2}{\lambda} + L }\\ T_{c2} &= T_c(0) = T_{c1} + \frac{L}{\frac{2}{\lambda} + L} (T_{h1} - T_{c1}) \end{aligned} in the limiting case L L \to \infty we get T c 2 = T h 1 T_{c2} = T_{h1} , so that the cold water stream can get as hot as the incoming hot water.

Parallel Flow

d T h d x + d T c d x = 0 \frac{dT_h}{dx} + \frac{dT_c}{dx} = 0 applies, so that the mean temperature T m = ( T h + T c ) / 2 = const T_m = (T_{h} + T_{c})/2 = \text{const} stays constant. Therefore, only the temperature difference Δ T ( x ) = T h ( x ) T c ( x ) \Delta T(x) = T_h(x) - T_c(x) must be considered, so that differential equation becomes onedimensional Δ T ( x ) = λ Δ T ( x ) \Delta T'(x) = - \lambda \Delta T(x) which is solved by Δ T ( x ) = ( T h 1 T c 1 ) exp ( λ x ) \Delta T(x) = (T_{h1} - T_{c1}) \exp(-\lambda x) . The final temperature of the cold stream results to T c 2 = T h 1 + T c 1 2 T h 1 T c 1 2 e λ L T_{c2} = \frac{T_{h1} + T_{c1}}{2} - \frac{T_{h1} - T_{c1}}{2} e^{-\lambda L} in the limit L L \to \infty we get T c 2 = T m T_{c2} = T_m , so that cold water stream can never exceed the mean temperature.

Plotting both final temperature as function of the length L L results T c 2 countercurrent ( L ) > T c 2 parallel ( L ) T_{c2}^\text{countercurrent}(L) > T_{c2}^\text{parallel}(L) for all L > 0 L > 0 , so that the countercurrent configuration is always more effective.

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