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A double-pipe parallel-flow heat exchanger is used to heat cold tap water with hot water. Hot water $\left(c_{p}=4.25 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( enters the tube at \)85^{\circ} \mathrm{C}$ at a rate of \(1.4 \mathrm{~kg} / \mathrm{s}\) and leaves at \(50^{\circ} \mathrm{C}\). The heat exchanger is not well insulated, and it is estimated that 3 percent of the heat given up by the hot fluid is lost from the heat exchanger. If the overall heat transfer coefficient and the surface area of the heat exchanger are \(1150 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and $4 \mathrm{~m}^{2}$, respectively, determine the rate of heat transfer to the cold water and the log mean temperature difference for this heat exchanger.

Short Answer

Expert verified
The rate of heat transfer to the cold water in this heat exchanger is 201,922.5 W. 2. What is the log mean temperature difference (LMTD) for this heat exchanger? The log mean temperature difference (LMTD) for this heat exchanger is 43.76°C.

Step by step solution

01

Calculate heat transfer rate from the hot fluid

Calculate the heat transfer rate from the hot fluid using the mass flow rate, specific heat, and temperature difference. Formulation: $$q_\text{hot} = m_\text{hot} \cdot c_{p,\text{hot}} \cdot \Delta T_\text{hot} $$ Where: \(q_\text{hot}\): Heat transfer rate from the hot fluid (in Watts) \(m_\text{hot}\): Mass flow rate of the hot fluid, which is \(1.4\) kg/s \(c_{p,\text{hot}}\): Specific heat of the hot fluid, which is \(4.25\) kJ/kg·K (convert it to \(4250\) J/kg·K) \(\Delta T_\text{hot}\): Hot fluid temperature difference, which is \(85 - 50 = 35\) °C Calculating, we have: $$q_\text{hot} = 1.4 \cdot 4250 \cdot 35$$ $$q_\text{hot} = 208250~W$$
02

Calculate heat transfer rate to the cold water

Calculate the heat transfer rate to the cold water by accounting for the 3% heat loss from the hot fluid: $$q_\text{cold} = 0.97 \times q_\text{hot}$$ Where, \(q_\text{cold}\): Heat transfer rate to the cold water (in Watts) Calculating, we have: $$q_\text{cold} = 0.97 \times 208250$$ $$q_\text{cold} = 201922.5~W$$
03

Calculate the log mean temperature difference (LMTD)

The LMTD for a parallel-flow heat exchanger is given by the formula: $$\text{LMTD} = \frac{\Delta T_1 - \Delta T_2}{\ln(\frac{\Delta T_1}{\Delta T_2})}$$ Where: \(\Delta T_1\): Temperature difference at one end of the heat exchanger \(\Delta T_2\): Temperature difference at the other end of the heat exchanger We know, \(q_\text{cold} = U \cdot A \cdot \text{LMTD}\), where \(U\) and \(A\) are the overall heat transfer coefficient and the surface area of the heat exchanger (\(1150~W/m^2·K\) and \(4~m^2\), respectively). Now we can solve for LMTD: $$\text{LMTD} = \frac{q_\text{cold}}{U \cdot A}$$ Substituting, $$\text{LMTD} = \frac{201922.5}{1150 \cdot 4}$$ $$\text{LMTD} = 43.76^{\circ}\mathrm{C}$$ So the rate of heat transfer to the cold water is \(201,922.5\) W, and the log mean temperature difference (LMTD) for this heat exchanger is \(43.76^{\circ}\mathrm{C}\).

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Most popular questions from this chapter

Consider a heat exchanger in which both fluids have the same specific heats but different mass flow rates. Which fluid will experience a larger temperature change: the one with the lower or higher mass flow rate?

A shell-and-tube heat exchanger with two shell passes and 12 tube passes is used to heat water $\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( in the tubes from \)20^{\circ} \mathrm{C}\( to \)70^{\circ} \mathrm{C}\( at a rate of \)4.5 \mathrm{~kg} / \mathrm{s}$. Heat is supplied by hot oil \(\left(c_{p}=2300 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) that enters the shell side at \(170^{\circ} \mathrm{C}\) at a rate of $10 \mathrm{~kg} / \mathrm{s}$. For a tube-side overall heat transfer coefficient of \(350 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine the heat transfer surface area on the tube side. Answer: \(25.7 \mathrm{~m}^{2}\)

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.

A counterflow heat exchanger is used to cool oil $\left(c_{p}=2.20 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( from \)110^{\circ} \mathrm{C}\( to \)85^{\circ} \mathrm{C}\( at a rate of \)0.75\( \)\mathrm{kg} / \mathrm{s}\( with cold water \)\left(c_{p}=4.18 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( that enters the heat exchanger at \)20^{\circ} \mathrm{C}$ at a rate of \(0.6 \mathrm{~kg} / \mathrm{s}\). If the overall heat transfer coefficient is \(800 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), the heat transfer area of the heat exchanger is (a) \(0.745 \mathrm{~m}^{2}\) (b) \(0.760 \mathrm{~m}^{2}\) (c) \(0.775 \mathrm{~m}^{2}\) (d) \(0.790 \mathrm{~m}^{2}\) (e) \(0.805 \mathrm{~m}^{2}\)

Cold water $\left(c_{p}=4.18 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( enters a crossflow heat exchanger at \)14^{\circ} \mathrm{C}\( at a rate of \)0.35 \mathrm{~kg} / \mathrm{s}$ where it is heated by hot air $\left(c_{p}=1.0 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( that enters the heat exchanger at \)65^{\circ} \mathrm{C}$ at a rate of \(0.8 \mathrm{~kg} / \mathrm{s}\) and leaves at $25^{\circ} \mathrm{C}$. Determine the maximum outlet temperature of the cold water and the effectiveness of this heat exchanger.

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