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Under what conditions is the heat transfer relation $$ \dot{Q}=\dot{m}_{c} c_{p c}\left(T_{c, \text { out }}-T_{c, \text { in }}\right)=\dot{m}_{h} c_{p h}\left(T_{h, \text { in }}-T_{h, \text { out }}\right) $$ valid for a heat exchanger?

Short Answer

Expert verified
Answer: The heat transfer relation is valid for a heat exchanger when the mass flow rates and specific heat capacities remain constant for both fluids, the fluids are single-phase, homogeneous mixtures, without phase changes or significant temperature-dependent specific heat capacities.

Step by step solution

01

Identify the terms in the heat transfer relation equation.

The given heat transfer equation is: $$ \dot{Q} = \dot{m}_c c_{p c} (T_{c, out} - T_{c, in}) = \dot{m}_h c_{p h} (T_{h, in} - T_{h, out}) $$ Where, \(\dot{Q}\) is the rate of heat transfer, \(\dot{m}_c\) and \(\dot{m}_h\) are the mass flow rates of the cold and hot fluids, respectively, \(c_{p c}\) and \(c_{p h}\) are the specific heat capacities of the cold and hot fluids, respectively, at constant pressure, \(T_{c, in}\) and \(T_{c, out}\) are the temperature of the cold fluid at the inlet and outlet, respectively, \(T_{h, in}\) and \(T_{h, out}\) are the temperature of the hot fluid at the inlet and outlet, respectively.
02

Identify the conditions when mass flow rates are constant.

The mass flow rates of both cold and hot fluids (\(\dot{m}_c\) and \(\dot{m}_h\)) must be constant for the given heat transfer relation to hold. This means that there should be no external forces, leaks, blockages or any other factors causing the mass flow rates to vary throughout the heat exchanger.
03

Identify the conditions when specific heat capacities are constant.

The specific heat capacities of both cold and hot fluids (\(c_{p c}\) and \(c_{p h}\)) must also be constant. This implies that both fluids should: 1. Be single-phase and homogeneous mixtures, and no phase changes (e.g., evaporation or condensation) should occur during the heat exchange process. 2. Have specific heat capacities that are not significantly dependent on temperature.
04

Identify the conditions for the validity of the heat transfer relation.

Based on the analysis in Steps 2 and 3, the heat transfer relation will be valid under the following conditions: 1. The mass flow rates of both cold and hot fluids must be constant, with no external forces, leaks, blockages, or any other factors causing variation. 2. The specific heat capacities of both cold and hot fluids must remain constant throughout the heat exchange process. 3. Both fluids should be single-phase and homogeneous mixtures, with no phase changes occurring during the heat exchange process. 4. The specific heat capacities of both fluids should not be significantly dependent on temperature. In conclusion, the heat transfer relation is valid for a heat exchanger when the mass flow rates and specific heat capacities remain constant for both fluids, and the fluids are single-phase, homogeneous mixtures, without phase changes or significant temperature-dependent specific heat capacities.

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Most popular questions from this chapter

The National Sanitation Foundation (NSF) standard for commercial warewashing equipment (ANSL/NSF 3) requires that the final rinse water temperature be between 82 and \(90^{\circ} \mathrm{C}\). A shell-and-tube heat exchanger is to heat \(0.5 \mathrm{~kg} / \mathrm{s}\) of water $\left(c_{p}=4200 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( from 48 to \)86^{\circ} \mathrm{C}$ by geothermal brine flowing through a single shell pass. The heated water is then fed into commercial warewashing equipment. The geothermal brine enters and exits the heat exchanger at 98 and \(90^{\circ} \mathrm{C}\), respectively. The water flows through four thin-walled tubes, each with a diameter of $25 \mathrm{~mm}$, with all four tubes making the same number of passes through the shell. The tube length per pass for each tube is \(5 \mathrm{~m}\). The corresponding convection heat transfer coefficients on the outer and inner tube surfaces are 1050 and $2700 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, respectively. The estimated fouling factor caused by the accumulation of deposit from the geothermal brine is $0.0002 \mathrm{~m}^{2} . \mathrm{K} / \mathrm{W}$. Determine the number of passes required for the tubes inside the shell to heat the water to \(86^{\circ} \mathrm{C}\), within the temperature range required by the ANIS/NSF 3 standard.

A shell-and-tube heat exchanger with two shell passes and eight tube passes is used to heat ethyl alcohol $\left(c_{p}=2670 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( in the tubes from \)25^{\circ} \mathrm{C}\( to \)70^{\circ} \mathrm{C}\( at a rate of \)2.1 \mathrm{~kg} / \mathrm{s}$. The heating is to be done by water $\left(c_{p}=4190 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( that enters the shell at \)95^{\circ} \mathrm{C}$ and leaves at \(60^{\circ} \mathrm{C}\). If the overall heat transfer coefficient is $800 \mathrm{~W} / \mathrm{m}^{2} . \mathrm{K}$, determine the heat transfer surface area of the heat exchanger using \((a)\) the LMTD method and \((b)\) the \(\varepsilon-\mathrm{NTU}\) method. Answer: \((a) 11.4 \mathrm{~m}^{2}\)

Can the temperature of the hot fluid drop below the inlet temperature of the cold fluid at any location in a heat exchanger? Explain.

Saturated water vapor at \(40^{\circ} \mathrm{C}\) is to be condensed as it flows through the tubes of an air-cooled condenser at a rate of $0.2 \mathrm{~kg} / \mathrm{s}$. The condensate leaves the tubes as a saturated liquid at \(40^{\circ} \mathrm{C}\). The rate of heat transfer to air is (a) \(34 \mathrm{~kJ} / \mathrm{s}\) (b) \(268 \mathrm{~kJ} / \mathrm{s}\) (c) \(453 \mathrm{~kJ} / \mathrm{s}\) (d) \(481 \mathrm{~kJ} / \mathrm{s}\) (e) \(515 \mathrm{~kJ} / \mathrm{s}\)

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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