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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 $5000 \mathrm{~kg} / \mathrm{h}\( of air \)\left(c_{p}=1.0 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( which enters the air handler at \)25^{\circ} \mathrm{C}$. If these streams are in counterflow and the water-stream conditions remain fixed, the minimum temperature at the air outlet is (a) \(5^{\circ} \mathrm{C}\) (b) \(12^{\circ} \mathrm{C}\) (c) \(19^{\circ} \mathrm{C}\) (d) \(22^{\circ} \mathrm{C}\) (e) \(25^{\circ} \mathrm{C}\)

Short Answer

Expert verified
Answer: (b) 12°C

Step by step solution

01

Calculate the heat transfer from the water stream

We can determine the heat transfer, Q, from the water stream using the equation: Q = m_water * c_p_water * (T_out_water - T_in_water) where m_water is the flow rate of water, c_p_water is the specific heat capacity of water, T_out_water is the leaving temperature of the water, and T_in_water is the entering temperature of the water. Given values: m_water = 1000 kg/h c_p_water = 4.2 kJ/(kg.K) T_in_water = 5°C T_out_water = 12°C Now, we can plug these values into the equation to obtain the heat transfer: Q = 1000 * 4.2 * (12 - 5) Q = 4200 * 7 Q = 29400 kJ/h
02

Calculate the heat gained by the air stream

Using the heat transfer, Q, and given information about the air stream, we'll find the final air temperature (T_out_air) using the equation: Q = m_air * c_p_air * (T_out_air - T_in_air) where m_air is the mass flow rate of air, c_p_air is the specific heat capacity of air, T_in_air is the entering temperature of the air, and T_out_air is the leaving temperature of the air. Given values: Q = 29400 kJ/h (from step 1) m_air = 5000 kg/h c_p_air = 1.0 kJ/(kg.K) T_in_air = 25°C Now, we can rearrange the equation to solve for T_out_air: T_out_air = Q / (m_air * c_p_air) + T_in_air T_out_air = 29400 / (5000 * 1) + 25 T_out_air = 5.88 + 25 T_out_air = 30.88°C Since these streams are in counterflow and the water-stream conditions remain fixed, the minimum temperature at the air outlet is the same as the outlet temperature of the water stream, which is 12°C. The correct answer is: (b) \(12^{\circ} \mathrm{C}\)

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Most popular questions from this chapter

Consider a water-to-water counterflow heat exchanger with these specifications. Hot water enters at \(90^{\circ} \mathrm{C}\) while cold water enters at \(20^{\circ} \mathrm{C}\). The exit temperature of the hot water is \(15^{\circ} \mathrm{C}\) greater than that of the cold water, and the mass flow rate of the hot water is 50 percent greater than that of the cold water. The product of heat transfer surface area and the overall heat transfer coefficient is \(2200 \mathrm{~W} / \mathrm{K}\). Taking the specific heat of both cold and hot water to be $c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\(, determine \)(a)\( the outlet temperature of the cold water, \)(b)$ the effectiveness of the heat exchanger, \((c)\) the mass flow rate of the cold water, and \((d)\) the heat transfer rate.

In a one-shell and eight-tube-pass heat exchanger, the temperature of water flowing at rate of \(50,000 \mathrm{lbm} / \mathrm{h}\) is raised from \(70^{\circ} \mathrm{F}\) to \(150^{\circ} \mathrm{F}\). Hot air $\left(c_{p}=0.25 \mathrm{Btu} / \mathrm{bm}{ }^{\circ} \mathrm{F}\right)$ that flows on the tube side enters the heat exchanger at \(600^{\circ} \mathrm{F}\) and exits at \(300^{\circ} \mathrm{F}\). If the convection heat transfer coefficient on the outer surface of the tubes is $30 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2},{ }^{\circ} \mathrm{F}$, determine the surface area of the heat exchanger using both LMTD and \(\varepsilon-\mathrm{NTU}\) methods. Account for the possible fouling resistance of \(0.0015\) and $0.001 \mathrm{~h} \cdot \mathrm{ft}^{2}+{ }^{\circ} \mathrm{F} /$ Btu on the water and air sides, respectively.

A one-shell-pass and eight-tube-passes heat exchanger is used to heat glycerin $\left(c_{p}=0.60 \mathrm{Btu} / \mathrm{lbm} \cdot{ }^{\circ} \mathrm{F}\right)\( from \)80^{\circ} \mathrm{F}\( to \)140^{\circ} \mathrm{F}$ by hot water $\left(c_{p}=1.0 \mathrm{Btu} / \mathrm{lbm} \cdot{ }^{\circ} \mathrm{F}\right)\( that enters the thin-walled \)0.5$-in-diameter tubes at \(175^{\circ} \mathrm{F}\) and leaves at \(120^{\circ} \mathrm{F}\). The total length of the tubes in the heat exchanger is \(400 \mathrm{ft}\). The convection heat transfer coefficient is $4 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}\( on the glycerin (shell) side and \)50 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}$ on the water (tube) side. Determine the rate of heat transfer in the heat exchanger \((a)\) before any fouling occurs and \((b)\) after fouling with a fouling factor of \(0.002 \mathrm{~h} \cdot \mathrm{ft}^{2}-\mathrm{F} / \mathrm{B}\) tu on the outer surfaces of the tubes.

Air \(\left(c_{p}=1005 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters a crossflow heat exchanger at \(20^{\circ} \mathrm{C}\) at a rate of $3 \mathrm{~kg} / \mathrm{s}$, where it is heated by a hot water stream \(\left(c_{p}=4190 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) that enters the heat exchanger at \(70^{\circ} \mathrm{C}\) at a rate of $1 \mathrm{~kg} / \mathrm{s}$. Determine the maximum heat transfer rate and the outlet temperatures of both fluids for that case.

Geothermal water $\left(c_{p}=4250 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( at \)75^{\circ} \mathrm{C}$ is to be used to heat fresh water \(\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) at \(17^{\circ} \mathrm{C}\) at a rate of \(1.2 \mathrm{~kg} / \mathrm{s}\) in a double-pipe counterflow heat exchanger. The heat transfer surface area is $25 \mathrm{~m}^{2}\(, the overall heat transfer coefficient is \)480 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, and the mass flow rate of geothermal water is larger than that of fresh water. If the effectiveness of the heat exchanger must be \(0.823\), determine the mass flow rate of geothermal water and the outlet temperatures of both fluids.

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