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?
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The local heat transfer rate for both streams read c V ˙ d x d T h d x ± c V ˙ d x d T c d x = − d Q ˙ = − k w ( T h ( x ) − T c ( x ) ) d x = d Q ˙ = k w ( T h ( x ) − T c ( x ) ) d x 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 ˙ we get the coupled differential equations ( − T h ′ ( x ) ± T c ′ ( x ) ) = 2 λ ( 1 1 − 1 − 1 ) ( T h ( x ) ± T c ( x ) )
Countercurrent Flow
d x d T h = d x d T c applies, so that the gradient T h ( x ) − T c ( x ) = Δ T results a constant. Therefore, the functions show a linear course T h ( x ) T c ( x ) = T h 1 − a x = T c 1 + a ( L − x ) with Δ T = T h 1 − T c 1 − a L = − ( 2 / λ ) ⋅ T h ′ ( x ) = 2 a / λ , so that a T c 2 = λ 2 + L T h 1 − T c 1 = T c ( 0 ) = T c 1 + λ 2 + L L ( T h 1 − T c 1 ) in the limiting case L → ∞ we get T c 2 = T h 1 , so that the cold water stream can get as hot as the incoming hot water.
Parallel Flow
d x d T h + d x d T c = 0 applies, so that the mean temperature T m = ( T h + T c ) / 2 = const stays constant. Therefore, only the temperature difference Δ T ( x ) = T h ( x ) − T c ( x ) must be considered, so that differential equation becomes onedimensional Δ T ′ ( x ) = − λ Δ T ( x ) which is solved by Δ T ( x ) = ( T h 1 − T c 1 ) exp ( − λ x ) . The final temperature of the cold stream results to T c 2 = 2 T h 1 + T c 1 − 2 T h 1 − T c 1 e − λ L in the limit L → ∞ we get T c 2 = T m , so that cold water stream can never exceed the mean temperature.
Plotting both final temperature as function of the length L results T c 2 countercurrent ( L ) > T c 2 parallel ( L ) for all L > 0 , so that the countercurrent configuration is always more effective.