Chapter 11: Problem 29
What are the common approximations made in the analysis of heat exchangers?
Chapter 11: Problem 29
What are the common approximations made in the analysis of heat exchangers?
All the tools & learning materials you need for study success - in one app.
Get started for freeDiscuss the differences between the cardiovascular countercurrent design and standard engineering countercurrent designs.
In a parallel-flow, liquid-to-liquid heat exchanger, the inlet and outlet temperatures of the hot fluid are \(150^{\circ} \mathrm{C}\) and $90^{\circ} \mathrm{C}\( while those of the cold fluid are \)30^{\circ} \mathrm{C}$ and \(70^{\circ} \mathrm{C}\), respectively. For the same overall heat transfer coefficient, the percentage decrease in the surface area of the heat exchanger if counterflow arrangement is used is (a) \(3.9 \%\) (b) \(9.7 \%\) (c) \(14.5 \%\) (d) \(19.7 \%\) (e) \(24.6 \%\)
Cold water $\left(c_{p}=4.18 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( enters a counterflow heat exchanger at \)18^{\circ} \mathrm{C}\( at a rate of \)0.7 \mathrm{~kg} / \mathrm{s}$ where it is heated by hot air \(\left(c_{p}=1.0 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\) that enters the heat exchanger at \(50^{\circ} \mathrm{C}\) at a rate of $1.6 \mathrm{~kg} / \mathrm{s}\( and leaves at \)25^{\circ} \mathrm{C}$. The maximum possible outlet temperature of the cold water is (a) \(25.0^{\circ} \mathrm{C}\) (b) \(32.0^{\circ} \mathrm{C}\) (c) \(35.5^{\circ} \mathrm{C}\) (d) \(39.7^{\circ} \mathrm{C}\) (e) \(50.0^{\circ} \mathrm{C}\)
In a chemical plant, a certain chemical is heated by hot water supplied by a natural gas furnace. The hot water $\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( is then discharged at \)60^{\circ} \mathrm{C}$ at a rate of \(8 \mathrm{~kg} / \mathrm{min}\). The plant operates \(8 \mathrm{~h}\) a day, 5 days a week, 52 weeks a year. The furnace has an efficiency of 78 percent, and the cost of the natural gas is \(\$ 1.00\) per therm ( 1 therm \(=105,500 \mathrm{~kJ}\) ). The average temperature of the cold water entering the furnace throughout the year is \(14^{\circ} \mathrm{C}\). In order to save energy, it is proposed to install a water-to-water heat exchanger to preheat the incoming cold water with the drained hot water. Assuming that the heat exchanger will recover 72 percent of the available heat in the hot water, determine the heat transfer rating of the heat exchanger that needs to be purchased, and suggest a suitable type. Also, determine the amount of money this heat exchanger will save the company per year from natural gas savings.
A single-pass crossflow heat exchanger with both fluids unmixed has water entering at \(16^{\circ} \mathrm{C}\) and exiting at \(33^{\circ} \mathrm{C}\), while oil $\left(c_{p}=1.93 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right.\( and \)\left.\rho=870 \mathrm{~kg} / \mathrm{m}^{3}\right)$ flowing at \(0.19 \mathrm{~m}^{3} / \mathrm{min}\) enters at $38^{\circ} \mathrm{C}\( and exits at \)29^{\circ} \mathrm{C}$. If the surface area of the heat exchanger is \(20 \mathrm{~m}^{2}\), determine \((a)\) the NTU value and \((b)\) the value of the overall heat transfer coefficient.
What do you think about this solution?
We value your feedback to improve our textbook solutions.