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An air handler is a large unmixed heat exchanger used for comfort control in large buildings. In one such application, chilled water $\left(c_{p}=4.2 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)$ enters an air handler at \(5^{\circ} \mathrm{C}\) and leaves at \(12^{\circ} \mathrm{C}\) with a flow rate of \(1000 \mathrm{~kg} / \mathrm{h}\). This cold water cools air \(\left(c_{p}=1.0 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\) from \(25^{\circ} \mathrm{C}\) to \(15^{\circ} \mathrm{C}\). The rate of heat transfer between the two streams is (a) \(8.2 \mathrm{~kW}\) (b) \(23.7 \mathrm{~kW}\) (c) \(33.8 \mathrm{~kW}\) (d) \(44.8 \mathrm{~kW}\) (e) \(52.8 \mathrm{~kW}\)

Short Answer

Expert verified
Answer: (a) 8.2 kW

Step by step solution

01

Convert flow rate of chilled water to kg/s

We are given the flow rate of the chilled water in kg/h. To make the calculations easier, let's convert this flow rate to kg/s. \(Flow\,rate\,in\,kg/s = \frac{1000 \, kg/h}{3600 \, s}\)
02

Calculate heat gained by the chilled water

To find the heat gained by the chilled water, we can use the following equation: \(Q_{water} = m_{water} \cdot c_{p_{water}} \cdot \Delta T_{water}\) where \(Q_{water}\) is the heat gained by the chilled water, \(m_{water}\) is the mass flow rate of the chilled water in kg/s, \(c_{p_{water}}\) is the specific heat capacity of the water in kJ/(kg·K), and \(\Delta T_{water}\) is the temperature change of the water in K. We have values for all the variables, so we can put them into the equation: \(Q_{water} = \frac{1000}{3600} \cdot 4.2 \cdot (12 - 5)\)
03

Calculate heat lost by the air

Since the heat transferred between the two streams must be equal, the heat lost by the air can be found by setting the heat gained by the chilled water equal to the heat loss by the air: \(Q_{air} = Q_{water}\) We must now find the mass flow rate of the air using the following equation: \(Q_{air} = m_{air} \cdot c_{p_{air}} \cdot \Delta T_{air}\) where \(Q_{air}\) is the heat transmitted from the air, \(m_{air}\) is the mass flow rate of the air in kg/s, \(c_{p_{air}}\) is the specific heat capacity of the air in kJ/(kg·K), and \(\Delta T_{air}\) is the temperature change of the air in K. We know the specific heat capacity and temperature change of the air. Let's put everything into the equation: \(\frac{1000}{3600} \cdot 4.2 \cdot (12 - 5) = m_{air} \cdot 1.0 \cdot (25 - 15)\)
04

Solve for the rate of heat transfer

Now that we have the equations set up, we can solve for the rate of heat transfer between the two streams. The heat gained by the chilled water is equal to the heat lost by the air: \(Q_{water} = Q_{air}\) \(\frac{1000}{3600} \cdot 4.2 \cdot (12 - 5) = m_{air} \cdot 1.0 \cdot (25 - 15)\) We can now solve for \(Q_{water}\), which is also the rate of heat transfer between the two streams: \(Q_{water} = 0.278 \times 29.4 = 8.1732 \, kW\) This value is closest to option (a), so the answer is: (a) \(8.2 \mathrm{~kW}\)

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Most popular questions from this chapter

Describe the cardiovascular countercurrent mechanism in the human body.

Water \(\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters the \(2.5\)-cm-internaldiameter tube of a double-pipe counterflow heat exchanger at \(20^{\circ} \mathrm{C}\) at a rate of $2.2 \mathrm{~kg} / \mathrm{s}\(. Water is heated by steam condensing at \)120^{\circ} \mathrm{C}\left(h_{f g}=2203 \mathrm{~kJ} / \mathrm{kg}\right)$ in the shell. If the overall heat transfer coefficient of the heat exchanger is $700 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, determine the length of the tube required in order to heat the water to \(80^{\circ} \mathrm{C}\) using \((a)\) the LMTD method and \((b)\) the \(\varepsilon-\mathrm{NTU}\) method.

Cold water $\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)$ leading to a shower enters a thin-walled double-pipe counterflow heat exchanger at \(15^{\circ} \mathrm{C}\) at a rate of $0.25 \mathrm{~kg} / \mathrm{s}\( and is heated to \)45^{\circ} \mathrm{C}$ by hot water \(\left(c_{p}=4190 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) that enters at \(100^{\circ} \mathrm{C}\) at a rate of $3 \mathrm{~kg} / \mathrm{s}\(. If the overall heat transfer coefficient is \)950 \mathrm{~W} / \mathrm{m}^{2}\(. \)\mathrm{K}$, determine the rate of heat transfer and the heat transfer surface area of the heat exchanger using the \(\varepsilon-\mathrm{NTU}\) method. Answers: \(31.35 \mathrm{~kW}\), $0.482 \mathrm{~m}^{2}$

Air at $18^{\circ} \mathrm{C}\left(c_{p}=1006 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( is to be heated to \)58^{\circ} \mathrm{C}$ by hot oil at $80^{\circ} \mathrm{C}\left(c_{p}=2150 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)$ in a crossflow heat exchanger with air mixed and oil unmixed. The product of the heat transfer surface area and the overall heat transfer coefficient is \(750 \mathrm{~W} / \mathrm{K}\), and the mass flow rate of air is twice that of oil. Determine \((a)\) the effectiveness of the heat exchanger, (b) the mass flow rate of air, and (c) the rate of heat transfer.

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) \(1.0\)

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