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 counter-flow 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: (c) \(19^{\circ} \mathrm{C}\)

Step by step solution

01

Recall energy balance equation

The energy balance equation states that the energy entering or leaving a system must be equal to the energy entering or leaving it. For this problem, we can apply an energy balance on the air side, assuming no additional energy is exchanged with the surroundings: \(\dot{m}_{air} c_{p, air} (T_{in, air} - T_{out, air}) = \dot{m}_{water} c_{p, water} (T_{in, water} - T_{out, water})\) where \(\dot{m}_{air}\) and \(\dot{m}_{water}\) are the mass flow rates of the air and water respectively; \(c_{p, air}\) and \(c_{p, water}\) are the specific heat capacities of air and water, respectively; and \(T_{in, air}\), \(T_{out, air}\), \(T_{in, water}\), and \(T_{out, water}\) are the inlet and outlet temperatures of the air and water, respectively.
02

Plug in the given values and solve for the unknown

The mass flow rates of air and water are given, as well as their respective specific heat capacities and inlet and outlet temperatures. Using these values and plugging them into the energy balance equation, we have: \((5000 \mathrm{~kg} / \mathrm{h}) (1.0 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K})(25^{\circ} \mathrm{C} - T_{out, air}) = (1000 \mathrm{~kg} / \mathrm{h}) (4.2 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K})(5^{\circ} \mathrm{C} - 12^{\circ} \mathrm{C})\) Now we can solve for the unknown temperature \(T_{out, air}\): \(5000(25 - T_{out, air}) = -1000(4.2)(5 - 12)\) \(125000 - 5000 T_{out, air} = 29400\) \(-5000 T_{out, air} = -95500\) \(T_{out, air} = 19.1^{\circ} \mathrm{C}\) Since the air is cooled in a heat exchanger, it is not possible to obtain a lower temperature at the air outlet because the water temperature is fixed. Therefore, the minimum temperature at the air outlet is (c) \(19^{\circ} \mathrm{C}\).

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Most popular questions from this chapter

The radiator in an automobile is a cross-flow heat exchanger \(\left(U A_{s}=10 \mathrm{~kW} / \mathrm{K}\right)\) that uses air \(\left(c_{p}=1.00 \mathrm{~kJ} /\right.\) \(\mathrm{kg} \cdot \mathrm{K})\) to \(\mathrm{cool}\) the engine coolant fluid \(\left(c_{p}=4.00 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\). The engine fan draws \(30^{\circ} \mathrm{C}\) air through this radiator at a rate of \(10 \mathrm{~kg} / \mathrm{s}\) while the coolant pump circulates the engine coolant at a rate of \(5 \mathrm{~kg} / \mathrm{s}\). The coolant enters this radiator at \(80^{\circ} \mathrm{C}\). Under these conditions, what is the number of transfer units (NTU) of this radiator? (a) 1 (b) 2 (c) 3 (d) 4 (e) 5

Water \(\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters the \(2.5\)-cm-internaldiameter tube of a double-pipe counter-flow heat exchanger at \(17^{\circ} \mathrm{C}\) at a rate of \(1.8 \mathrm{~kg} / \mathrm{s}\). 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.

A 1-shell-pass and 8-tube-passes heat exchanger is used to heat glycerin \(\left(c_{p}=0.60 \mathrm{Btu} / \mathrm{lbm} \cdot{ }^{\circ} \mathrm{F}\right)\) from \(65^{\circ} \mathrm{F}\) 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 thinwalled \(0.5\)-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 \(500 \mathrm{ft}\). The convection heat transfer coefficient is \(4 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F}\) on the glycerin (shell) side and \(50 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F}\) 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 \(0.002 \mathrm{~h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F} /\) Btu on the outer surfaces of the tubes.

Consider a heat exchanger that has an NTU of 4 . Someone proposes to double the size of the heat exchanger and thus double the NTU to 8 in order to increase the effectiveness of the heat exchanger and thus save energy. Would you support this proposal?

For a specified fluid pair, inlet temperatures, and mass flow rates, what kind of heat exchanger will have the highest effectiveness: double-pipe parallel- flow, double-pipe counterflow, cross-flow, or multipass shell-and-tube heat exchanger?

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