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What is the physical significance of the number of transfer units \(\mathrm{NTU}=h A_{s} / \dot{m} c_{p}\) ? What do small and large NTU values tell us about a heat transfer system?

Short Answer

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Answer: The NTU in a heat transfer system can be affected by factors such as heat transfer surface area, heat transfer coefficient, and mass flow rate. Small heat transfer surface area, poor heat transfer coefficient, and high mass flow rate can result in a lower NTU, indicating a less effective heat transfer system. On the other hand, large heat transfer surface area, high heat transfer coefficient, and low mass flow rate can lead to a higher NTU, indicating a highly effective heat transfer system.

Step by step solution

01

Defining the terms in the NTU formula

The NTU formula is given as \(\mathrm{NTU}=h A_{s} / \dot{m} c_{p}\), where: - \(NTU\): Number of Transfer Units, a dimensionless number - \(h\): Heat transfer coefficient (W/m²K) - \(A_s\): Heat transfer surface area (m²) - \(\dot{m}\): Mass flow rate (kg/s) - \(c_p\): Specific heat capacity of the fluid at constant pressure (J/kgK) The NTU (Number of Transfer Units) quantifies how effective a heat exchanger is in transferring heat between two fluids.
02

Significance of NTU

The NTU is a measure of the "thermal size" of a heat exchanger, which accounts for its ability to transfer heat from one fluid to another. A high NTU indicates that the exchanger is highly effective in transferring heat between the two fluids, while a low NTU means that the exchanger is less effective in transferring heat.
03

Small NTU values

Small NTU values indicate that the heat exchanger is relatively ineffective in transferring heat between the two fluids. This could be due to a variety of factors, such as: - Low heat transfer surface area: A smaller heat transfer surface area reduces the potential for heat to transfer between the fluids, resulting in a lower NTU value. - Poor heat transfer coefficient: A low heat transfer coefficient indicates that the heat transfer process is not as effective, likely due to a lower thermal conductivity of the materials involved or impeded heat transfer due to dirt, fouling, or other factors. - High mass flow rate: A high mass flow rate means the fluid is moving quickly through the system, which can limit the amount of time the fluid spends in the heat exchanger, reducing the opportunity for heat transfer to take place.
04

Large NTU values

Large NTU values indicate that the heat transfer system is highly effective in transferring heat between the fluids, which can be due to a variety of factors, such as: - Large heat transfer surface area: The larger the heat transfer surface area, the greater the potential for heat exchange between the fluids, leading to a higher NTU value. - High heat transfer coefficient: A high heat transfer coefficient indicates that the heat transfer process is more effective, which can be due to increased thermal conductivity for both the heat exchanger materials and the fluids themselves. - Low mass flow rate: If the mass flow rate is low, the fluid spends more time in the heat exchanger, allowing for more thorough heat exchange and thus increasing the NTU value. In conclusion, the Number of Transfer Units (NTU) is a significant parameter to characterize the performance of heat transfer systems. Small NTU values indicate less effective heat transfer systems, whereas large NTU values indicate highly effective heat transfer systems. By understanding the impact of the heat transfer surface area, heat transfer coefficient, and mass flow rate on NTU, we can design more efficient heat exchangers and optimize heat transfer system performance.

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Most popular questions from this chapter

Air is flowing through a smooth, thin-walled, 4-in-diameter copper tube that is submerged in water. The water maintains a constant temperature of \(60^{\circ} \mathrm{F}\) and a convection heat transfer coefficient of $176 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot \mathrm{R}\(. If air \)(1 \mathrm{~atm})\( enters the copper tube at a mean temperature of \)90^{\circ} \mathrm{F}\( with an average velocity of \)8 \mathrm{ft} / \mathrm{s}$, determine the necessary copper tube length so that the outlet mean temperature of the air is \(70^{\circ} \mathrm{F}\).

Liquid water flows in an ASTM B75 copper tube at a mass flow rate of $3.6 \mathrm{~g} / \mathrm{s}\(. The water enters the tube at \)40^{\circ} \mathrm{C}$, and the tube surface is subjected to a constant heat flux at a rate of \(1.8 \mathrm{~kW}\). The tube is circular with an inner diameter of $25 \mathrm{~mm}\( and a length of \)3 \mathrm{~m}$. The maximum use temperature for ASTM B75 copper tube is \(204^{\circ} \mathrm{C}\) (ASME Code for Process Piping, B31.3-2014, Table A-1M). Would the surface temperature of the tube exceed the maximum use temperature for the copper tube? If so, determine the axial location along the tube where the tube's surface temperature reaches \(204^{\circ} \mathrm{C}\). Evaluate the fluid properties at $100^{\circ} \mathrm{C}$. Is this an appropriate temperature at which to evaluate the fluid properties?

Water at \(15^{\circ} \mathrm{C}\) is flowing through a \(5-\mathrm{cm}\)-diameter smooth tube with a length of \(200 \mathrm{~m}\). Determine the Darcy friction factor and pressure loss associated with the tube for (a) mass flow rate of \(0.02 \mathrm{~kg} / \mathrm{s}\) and (b) mass flow rate of $0.5 \mathrm{~kg} / \mathrm{s}$.

Liquid water flows in a thin-walled circular tube, where the pumping power required to overcome the turbulent flow pressure loss in the tube is $100 \mathrm{~W}\(. The water enters the tube at \)10^{\circ} \mathrm{C}$, where it is heated at a rate of \(3.6 \mathrm{~kW}\). The average convection heat transfer coefficient for the internal flow is $120 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. The tube is \)3 \mathrm{~m}$ long and has an inner diameter of \(12.5 \mathrm{~mm}\). The tube surface is maintained at a constant temperature. At the tube exit, an ethylene propylene diene (EPDM) rubber o-ring is attached to the tube's outer surface. The maximum temperature permitted for the o-ring is \(150^{\circ} \mathrm{C}\) (ASME Boiler and Pressure Vessel Code, BPVC. IV-2015, HG-360). Is the EPDM o-ring suitable for this operation? Evaluate the fluid properties at \(10^{\circ} \mathrm{C}\). Is this an appropriate temperature at which to evaluate the fluid properties?

Air at \(110^{\circ} \mathrm{C}\) enters an \(18-\mathrm{cm}\)-diameter and \(9-\mathrm{m}\)-long duct at a velocity of \(4.5 \mathrm{~m} / \mathrm{s}\). The duct is observed to be nearly isothermal at \(85^{\circ} \mathrm{C}\). The rate of heat loss from the air in the duct is (a) \(760 \mathrm{~W}\) (b) \(890 \mathrm{~W}\) (c) \(1210 \mathrm{~W}\) (d) \(1370 \mathrm{~W}\) (e) \(1400 \mathrm{~W}\) (For air, use $k=0.03095 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \operatorname{Pr}=0.7111, \nu=2.306 \times\( \)10^{-5} \mathrm{~m}^{2} / \mathrm{s}, c_{p}=1009 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$.)

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