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A one-shell and two-tube-type heat exchanger has an overall heat transfer coefficient of $300 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}\(. The shell-side fluid has a heat capacity rate of \)20,000 \mathrm{Btu} / \mathrm{h} \cdot{ }^{\circ} \mathrm{F}$, while the tube-side fluid has a heat capacity rate of 40,000 $\mathrm{Btu} / \mathrm{h} \cdot{ }^{\circ} \mathrm{F}$. The inlet temperatures on the shell side and tube side are \(200^{\circ} \mathrm{F}\) and \(90^{\circ} \mathrm{F}\), respectively. If the total heat transfer area is \(100 \mathrm{ft}^{2}\), determine \((a)\) the heat transfer effectiveness and \((b)\) the actual heat transfer rate in the heat exchanger.

Short Answer

Expert verified
The heat transfer effectiveness is 0.719, and the actual heat transfer rate is 1,584,900 Btu/h.

Step by step solution

01

Calculate the Minimum Fluid Heat Capacity Rate (C\(_{min}\))

First, we need to find the minimum fluid heat capacity rate, which will be the smaller value between the shell-side heat capacity rate (C\(_{s}\)) and the tube-side heat capacity rate (C\(_{t}\)). C\(_{min}\) = min(C\(_{s}\), C\(_{t}\)) = min(\(20,000 \mathrm{Btu/h\cdot^\circ F}\), \(40,000 \mathrm{Btu/h\cdot^\circ F}\)) = \(20,000 \mathrm{Btu/h\cdot^\circ F}\)
02

Calculate the Number of Transfer Units (NTU)

Next, we will calculate the number of transfer units (NTU) using the given overall heat transfer coefficient (U), total heat transfer area (A), and the minimum fluid heat capacity rate (C\(_{min}\)): NTU = \frac{UA}{C_{min}} = \frac{300 \mathrm{Btu/h\cdot ft^2\cdot^\circ F} \cdot 100 \mathrm{ft^2}}{20,000 \mathrm{Btu/h\cdot^\circ F}} = 1.5
03

Calculate the heat transfer effectiveness (ε)

Now, we will calculate the heat transfer effectiveness (ε) for the one-shell and two-tube heat exchanger configuration using the NTU: ε = \frac{1 - e^{-NTU(1+C_r)} (1 + C_r)}{1 + C_r} = \frac{1 - e^{-1.5(1 + 0.5)} (1 + 0.5)}{1 + 0.5} = 0.719 where C\(_r\) = C\(_{min}\)/C\(_{max}\) = \(20,000 \mathrm{Btu/h\cdot}^\circ \mathrm{F}\)/ \(40,000 \mathrm{Btu/h\cdot}^\circ \mathrm{F}\) = 0.5 So, the heat transfer effectiveness is 0.719.
04

Calculate the actual heat transfer rate (Q)

Finally, we will calculate the actual heat transfer rate (Q) using the heat transfer effectiveness (ε) and the minimum fluid heat capacity rate (C\(_{min}\)): Q = εC\(_{min}\)ΔT\(_{in}\) = 0.719 × \(20,000 \mathrm{Btu/h\cdot^\circ F}\) × (\(200^{\circ} \mathrm{F}\) - \(90^{\circ} \mathrm{F}\)) = 0.719 × \(20,000 \mathrm{Btu/h\cdot^\circ F}\) × \(110^{\circ} \mathrm{F}\) = 1,584,900 \mathrm{Btu/h} To summarize, the heat transfer effectiveness of the one-shell and two-tube-type heat exchanger is 0.719, and the actual heat transfer rate is 1,584,900 Btu/h.

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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.

An air-cooled condenser is used to condense isobutane in a binary geothermal power plant. The isobutane is condensed at \(85^{\circ} \mathrm{C}\) by air \(\left(c_{p}=1.0 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right.\) ) that enters at \(22^{\circ} \mathrm{C}\) at a rate of \(18 \mathrm{~kg} / \mathrm{s}\). The overall heat transfer coefficient and the surface area for this heat exchanger are \(2.4 \mathrm{~kW} / \mathrm{m}^{2} \cdot \mathrm{K}\) and $2.6 \mathrm{~m}^{2}$, respectively. The outlet temperature of the air is (a) \(35.6^{\circ} \mathrm{C}\) (b) \(40.5^{\circ} \mathrm{C}\) (c) \(52.1^{\circ} \mathrm{C}\) (d) \(58.5^{\circ} \mathrm{C}\) (e) \(62.8^{\circ} \mathrm{C}\)

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

A two-shell-pass and four-tube-pass heat exchanger is used for heating a hydrocarbon stream $\left(c_{p}=2.0 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( steadily from \)20^{\circ} \mathrm{C}\( to \)50^{\circ} \mathrm{C}\(. A water stream enters the shell side at \)80^{\circ} \mathrm{C}$ and leaves at \(40^{\circ} \mathrm{C}\). There are 160 thin-walled tubes, each with a diameter of \(2.0 \mathrm{~cm}\) and length of \(1.5 \mathrm{~m}\). The tube-side and shell-side heat transfer coefficients are \(1.6\) and $2.5 \mathrm{~kW} / \mathrm{m}^{2} \cdot \mathrm{K}$, respectively. (a) Calculate the rate of heat transfer and the mass rates of water and hydrocarbon streams. (b) With usage, the outlet hydrocarbon-stream temperature was found to decrease by \(5^{\circ} \mathrm{C}\) due to the deposition of solids on the tube surface. Estimate the magnitude of the fouling factor.

Oil is being cooled from \(180^{\circ} \mathrm{F}\) to \(120^{\circ} \mathrm{F}\) in a oneshell and two-tube heat exchanger with an overall heat transfer coefficient of $40 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}\(. Water \)\left(c_{p c}=1.0 \mathrm{Btu} / \mathrm{lbm} \cdot{ }^{\circ} \mathrm{F}\right)\( enters at \)80^{\circ} \mathrm{F}$ and exits at \(100^{\circ} \mathrm{F}\) with a mass flow rate of $20,000 \mathrm{lbm} / \mathrm{h}\(. Determine \)(a)\( the NTU value and \)(b)$ the surface area of the heat exchanger.

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