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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?

Short Answer

Expert verified
Answer: The fluid with the lower mass flow rate will experience a larger temperature change than the one with the higher mass flow rate.

Step by step solution

01

Understand the concept of heat transfer in a heat exchanger

A heat exchanger is a device used to transfer heat between two or more fluids. The fluids in the heat exchanger have different temperatures, and heat transfer occurs from the hotter fluid to the cooler fluid until the temperature of the two fluids equalizes. In the given exercise, we are considering two fluids with the same specific heats but different mass flow rates.
02

Define the heat transfer equation

The heat transfer equation (Q) for a fluid can be expressed as: Q = m*c_p*ΔT Where, Q = heat transfer (J) m = mass flow rate of the fluid (kg/s) c_p = specific heat of the fluid (J/kg*K) ΔT = temperature change of the fluid (K)
03

Set up equations for both fluids in the heat exchanger

Let the mass flow rates be m1 and m2 for fluid 1 and fluid 2, respectively, with m1 ≠ m2. Let ΔT1 and ΔT2 be the temperature changes for fluid 1 and fluid 2. Since the heat transferred from fluid 1 to fluid 2 must be the same (assuming no heat loss to the surroundings and no heat stored in the heat exchanger itself), we can set the heat transfer equations for both fluids equal to each other: m1 * c_p * ΔT1 = m2 * c_p * ΔT2
04

Eliminate common terms and solve for temperature change

We can cancel out the common term c_p from both sides of the equation: m1 * ΔT1 = m2 * ΔT2 Now, we can divide both sides by m1 * m2: ΔT1 / m1 = ΔT2 / m2
05

Analyze the relationship between mass flow rate and temperature change

From the above equation, we can see that the temperature change of a fluid is inversely proportional to its mass flow rate, given the same heat transfer. Therefore, the fluid with the lower mass flow rate will experience a larger temperature change, while the fluid with the higher mass flow rate will experience a smaller temperature change. So, the fluid with the lower mass flow rate will experience a larger temperature change than the one with the higher mass flow rate.

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Most popular questions from this chapter

Water is boiled at \(150^{\circ} \mathrm{C}\) in a boiler by hot exhaust gases $\left(c_{p}=1.05 \mathrm{~kJ} / \mathrm{kg}^{\circ}{ }^{\circ} \mathrm{C}\right)\( that enter the boiler at \)540^{\circ} \mathrm{C}$ at a rate of \(0.4 \mathrm{~kg} / \mathrm{s}\) and leave at \(200^{\circ} \mathrm{C}\). The surface area of the heat exchanger is \(0.64 \mathrm{~m}^{2}\). The overall heat transfer coefficient of this heat exchanger is\(\mathrm{kg} / \mathrm{s}\) 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) \(0.805 \mathrm{~m}^{2}\)

A pipe system is mainly constructed with ASTM F441 CPVC pipes. The ASME Code for Process Piping (ASME B31.3-2014, Table B-1) recommends that the maximum temperature limit for CPVC pipes be \(93.3^{\circ} \mathrm{C}\). A double-pipe heat exchanger is located upstream of the pipe system to reduce the hot water temperature before it flows into the CPVC pipes. The inner tube of the heat exchanger has a negligible wall thickness, and its length and diameter are $5 \mathrm{~m}\( and \)25 \mathrm{~mm}$, respectively. The convection heat transfer coefficients inside and outside of the heat exchanger inner tube are $3600 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\( and \)4500 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, respectively. The hot fluid enters the heat exchanger at \(105^{\circ} \mathrm{C}\) with a flow rate of $0.75 \mathrm{~kg} / \mathrm{s}$. In the cold fluid stream, water enters the heat exchanger at \(10^{\circ} \mathrm{C}\) and exits at \(80^{\circ} \mathrm{C}\). Determine whether this double-pipe heat exchanger should employ the parallel flow or the counterflow configuration to ensure that the hot water exiting the heat exchanger is \(93.3^{\circ} \mathrm{C}\) or lower.

Write an interactive computer program that will give the effectiveness of a heat exchanger and the outlet temperatures of both the hot and cold fluids when the types of fluids, the inlet temperatures, the mass flow rates, the heat transfer surface area, the overall heat transfer coefficient, and the type of heat exchanger are specified. The program should allow the user to select from the fluids water, engine oil, glycerin, ethyl alcohol, and ammonia. Assume constant specific heats at about room temperature.

A shell-and-tube heat exchanger with two shell passes and four tube passes is used for cooling oil $\left(c_{p}=2.0 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( from \)125^{\circ} \mathrm{C}\( to \)55^{\circ} \mathrm{C}$. The coolant is water, which enters the shell side at \(25^{\circ} \mathrm{C}\) and leaves at \(46^{\circ} \mathrm{C}\). The overall heat transfer coefficient is \(900 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). For an oil flow rate of \(10 \mathrm{~kg} / \mathrm{s}\), calculate the cooling water flow rate and the heat transfer area.

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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