Chapter 11: Problem 93
How is the NTU of a heat exchanger defined? What does it represent? Is a heat exchanger with a very large NTU (say, 10 ) necessarily a good one to buy?
Chapter 11: Problem 93
How is the NTU of a heat exchanger defined? What does it represent? Is a heat exchanger with a very large NTU (say, 10 ) necessarily a good one to buy?
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Get started for freeConsider a heat exchanger that has an NTU of \(0.1\). Someone proposes to triple the size of the heat exchanger and thus triple the NTU to \(0.3\) in order to increase the effectiveness of the heat exchanger and thus save energy. Would you support this proposal?
Under what conditions can a counterflow heat exchanger have an effectiveness of 1 ? What would your answer be for a parallel-flow heat exchanger?
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?
A crossflow heat exchanger with both fluids unmixed has an overall heat transfer coefficient of \(200 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), and a heat transfer surface area of \(400 \mathrm{~m}^{2}\). The hot fluid has a heat capacity of \(40,000 \mathrm{~W} / \mathrm{K}\), while the cold fluid has a heat capacity of \(80,000 \mathrm{~W} / \mathrm{K}\). If the inlet temperatures of both hot and cold fluids are \(80^{\circ} \mathrm{C}\) and $20^{\circ} \mathrm{C}\(, respectively, determine \)(a)$ the exit temperature of the hot fluid and \((b)\) the rate of heat transfer in the heat exchanger.
A double-pipe heat exchanger is used to cool a hot fluid before it flows into a system of pipes. The inner surface of the pipes is primarily coated with polypropylene lining. The maximum use temperature for polypropylene lining is $107^{\circ} \mathrm{C}$ (ASME Code for Process Piping, ASME B31.32014, Table A323.4.3). The double-pipe heat exchanger has a thin-walled inner tube, with convection heat transfer coefficients inside and outside of the inner tube estimated to be \(1400 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and $1100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, respectively. The heat exchanger has a heat transfer surface area of \(2.5 \mathrm{~m}^{2}\), and the estimated fouling factor caused by the accumulation of deposit on the surface is \(0.0002\) \(\mathrm{m}^{2} \cdot \mathrm{K} / \mathrm{W}\). The hot fluid \(\left(c_{p}=3800 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters the heat exchanger at \(200^{\circ} \mathrm{C}\) with a flow rate of $0.4 \mathrm{~kg} / \mathrm{s}\(. In the cold side, cooling fluid \)\left(c_{p}=4200 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)$ enters the heat exchanger at \(10^{\circ} \mathrm{C}\) with a mass flow rate of $0.5 \mathrm{~kg} / \mathrm{s}$.
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