CENG 402 Heat Transfer Project

Parallel and CounterFlow Heat Exchangers

By: Ricardo Villanueva and Austin Hardin

This project describes the performance of the simple double-pipe heat exchanger shown in the following figure in terms of the heat-transfer coefficients of the two streams and the thermal resistance of the pipe wall. The exchanger consists essentially of two coaxial pipes with one fluid stream flowing through the inner pipe and another in the annular space; heat is transfered across the wall of the inner pipe. Both streams may flow in the same direction, as indicated in the figure, but normally it is more efficient to use counter flow, that is , to reverse the direction of one stream relative to the other. Steady state turbulent flow may be assumed, and heat losses to the surroundings may be neglected.

Double-pipe heat exchanger

Example 15.4-2 in BS&L

Sample Problem:

a.) Hot oil entering the heat exchanger in the above example at surface "2" is to be cooled by water entering at surface "1"; that is, the exchanger is being operated in counter flow. Compute the required exchanger area A if the heat-transfer coefficient U is 200 Btu/(hr* ft^2* F) and the fluid streams have the following properties:

Mass Flow Rate
lbm/hr
Heat Capacity
Btu/(lbm*F)
Temp. Entering
Temp. Leaving
Oil
12,000
0.60
250 F
150 F
Water
7,000
1.00
80 F
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b.) Repeat the calculation of part (a) if U1=50 and U2=350 Btu/(hr*ft^2*F). Assume that U varies linearly with water temperture, and use the following relation:


c.) What is the minimum amount of water that can be used in parts (a) and (b) to obtain the desired oil temperature change? What is the minimum amount of water that can be used in parallel flow?

d.) Calculate the required exchanger area for parallel flow operation if the mass rate of flow of water is 12,000 lbm/hr and U is constant at 200 Btu/(hr*ft^2*F).

Solution to Sample Problem