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Consider a double-pipe counterflow heat exchanger. In order to enhance heat transfer, the length of the heat exchanger is now doubled. Do you think its effectiveness will also double?

Short Answer

Expert verified
Answer: Doubling the length of a double-pipe counterflow heat exchanger does not double its effectiveness. Although the heat transfer area increases, the relationship between effectiveness and length is not directly proportional.

Step by step solution

01

Understand the heat exchanger effectiveness definition

Effectiveness is defined as the ratio of actual heat transfer to the maximum possible heat transfer. Mathematically, it can be represented as: Effectiveness = \(\frac{Q_{actual}}{Q_{max}}\) Where \(Q_{actual}\) is the actual heat transfer and \(Q_{max}\) is the maximum possible heat transfer.
02

Identify the heat exchanger equation

For a double-pipe counterflow heat exchanger, the heat exchanger equation can be represented as: \(Q = U \times A \times \Delta T_{lm}\) Where: - \(Q\) is the rate of heat transfer - \(U\) is the overall heat transfer coefficient - \(A\) is the heat transfer area - \(\Delta T_{lm}\) is the log mean temperature difference
03

Relate the heat exchanger equation to the effectiveness

We can express the effectiveness in terms of the heat exchanger equation components: Effectiveness = \(\frac{UA}{C_{min}}(1-e^{-\frac{UA}{C_{min}}})\) Where \(C_{min}\) is the minimum heat capacity rate of the two fluids in the heat exchanger.
04

Analyze the effectiveness when doubling the heat exchanger length

When the length of the heat exchanger is doubled, the heat transfer area (\(A\)) also doubles. Let's analyze the effectiveness for the new heat exchanger where the area is \(2A\): Effectiveness (\(2A\)) = \(\frac{2UA}{C_{min}}(1-e^{-\frac{2UA}{C_{min}}})\)
05

Compare the effectiveness of the original and doubled heat exchanger

Now we will determine if the effectiveness doubles when the length of the heat exchanger is doubled: Effectiveness ratio = \(\frac{Effectiveness (2A)}{Effectiveness (A)}\) Effectiveness ratio = \(\frac{\frac{2UA}{C_{min}}(1-e^{-\frac{2UA}{C_{min}}})}{\frac{UA}{C_{min}}(1-e^{-\frac{UA}{C_{min}}})}\) After simplifying the equation, we get: Effectiveness ratio ≠ 2 Since the effectiveness ratio is not equal to 2, it can be concluded that doubling the length of the heat exchanger does not double the effectiveness.

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Most popular questions from this chapter

A shell-and-tube heat exchanger is used for cooling $47 \mathrm{~kg} / \mathrm{s}\( of a process stream flowing through the tubes from \)160^{\circ} \mathrm{C}\( to \)100^{\circ} \mathrm{C}$. This heat exchanger has a total of 100 identical tubes, each with an inside diameter of \(2.5 \mathrm{~cm}\) and negligible wall thickness. The average properties of the process stream are: $\rho=950 \mathrm{~kg} / \mathrm{m}^{3}, k=0.50 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, c_{p}=3.5 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}$, and \(\mu=0.002 \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}\). The coolant stream is water \(c_{p}=4.18\) \(\mathrm{kJ} / \mathrm{kg} \cdot \mathrm{K}\) at a flow rate of \(66 \mathrm{~kg} / \mathrm{s}\) and an inlet temperature of $10^{\circ} \mathrm{C}$, which yields an average shell-side heat transfer coefficient of \(4.0 \mathrm{~kW} / \mathrm{m}^{2} . \mathrm{K}\). Calculate the tube length if the heat exchanger has \((a)\) one shell pass and one tube pass and \((b)\) one shell pass and four tube passes.

Under what conditions can a counterflow heat exchanger have an effectiveness of 1 ? What would your answer be for a parallel-flow heat exchanger?

In a one-shell and two-tube heat exchanger, cold water with inlet temperature of \(20^{\circ} \mathrm{C}\) is heated by hot water supplied at the inlet at \(80^{\circ} \mathrm{C}\). The cold and hot water flow rates are $5000 \mathrm{~kg} / \mathrm{h}\( and \)10,000 \mathrm{~kg} / \mathrm{h}$, respectively. If the shell-andtube heat exchanger has a \(U A_{s}\) value of \(11,600 \mathrm{~W} / \mathrm{K}\), determine the cold water and hot water outlet temperatures. Assume $c_{p c}=4178 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\( and \)c_{p t}=4188 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$.

Steam is to be condensed on the shell side of a twoshell-passes and eight- tube-passes condenser, with 20 tubes in each pass. Cooling water enters the tubes at a rate of \(2 \mathrm{~kg} / \mathrm{s}\). If the heat transfer area is \(14 \mathrm{~m}^{2}\) and the overall heat transfer coefficient is $1800 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, the effectiveness of this condenser is (a) \(0.70\) (b) \(0.80\) (c) \(0.90\) (d) \(0.95\) (e) \(1.0\)

Water \(\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) is to be heated by solarheated hot air $\left(c_{p}=1010 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)$ in a double-pipe counterflow heat exchanger. Air enters the heat exchanger at \(90^{\circ} \mathrm{C}\) at a rate of \(0.3 \mathrm{~kg} / \mathrm{s}\), while water enters at $22^{\circ} \mathrm{C}\( at a rate of \)0.1 \mathrm{~kg} / \mathrm{s}$. The overall heat transfer coefficient based on the inner side of the tube is given to be $80 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. The length of the tube is \)12 \mathrm{~m}\(, and the internal diameter of the tube is \)1.2 \mathrm{~cm}$. Determine the outlet temperatures of the water and the air.

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