A double-pipe heat exchanger is constructed of a copper \((k=380 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) inner tube of internal diameter \(D_{i}=\) \(1.2 \mathrm{~cm}\) and external diameter \(D_{o}=1.6 \mathrm{~cm}\) and an outer tube of diameter \(3.0 \mathrm{~cm}\). The convection heat transfer coefficient is reported to be \(h_{i}=700 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) on the inner surface of the tube and \(h_{o}=1400 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) on its outer surface. For a fouling factor \(R_{f, i}=0.0005 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\) on the tube side and \(R_{f, o}=\) \(0.0002 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\) on the shell side, determine \((a)\) the thermal resistance of the heat exchanger per unit length and \((b)\) the overall heat transfer coefficients \(U_{i}\) and \(U_{o}\) based on the inner and outer surface areas of the tube, respectively.

Short Answer

Expert verified
Question: Calculate the thermal resistance of the heat exchanger per unit length and the overall heat transfer coefficients based on the inner and outer surface areas, given the convection coefficients, fouling factors, and tube dimensions. Answer: To calculate the thermal resistance of the heat exchanger per unit length (R_tot) and the overall heat transfer coefficients (U_i and U_o), follow these steps: 1. Calculate the tube wall's thermal resistance per unit length (R_t) using the formula: \[ R_{t} = \frac{\ln\frac{D_{o}}{D_{i}}}{2 \pi k} \] 2. Calculate inner and outer convective resistance, considering fouling factors (R_i and R_o) using the formulas: \[ R_{i} = \frac{1}{h_{i} \pi D_{i}} + R_{f, i} \] and \[ R_{o} = \frac{1}{h_{o} \pi D_{o}} + R_{f, o} \] 3. Determine the total thermal resistance per unit length (R_tot) by adding up all the resistances: \[ R_{tot} = R_{i} + R_{t} + R_{o} \] 4. Calculate the overall heat transfer coefficients based on the inner and outer surface areas (U_i and U_o) using the formulas: \[ U_{i} = \frac{1}{R_{tot}} \pi D_{i} \] and \[ U_{o} = \frac{1}{R_{tot}} \pi D_{o} \ ] Plug in the given values and perform the calculations to obtain the thermal resistance of the heat exchanger per unit length (R_tot), and the overall heat transfer coefficients (U_i and U_o).

Step by step solution

01

Calculate the tube wall's thermal resistance per unit length

Finding the thermal resistance in the tube wall between the inner and outer surfaces: $$R_{t} = \frac{\ln\frac{D_{o}}{D_{i}}}{2 \pi k}$$ Where \(R_t\) is the tube wall's thermal resistance, \(k\) is the copper thermal conductivity, \(D_i\) is the inner diameter, and \(D_o\) is the outer diameter.
02

Calculate inner and outer convective resistance, considering fouling factors

We are given the convection coefficients (\(h_{i}\) and \(h_{o}\)) and fouling factors (\(R_{f, i}\) and \(R_{f, o}\)) for the heat exchanger. To account for fouling, we need to calculate the thermal resistance for both the inner and outer surfaces. For the inner surface: $$R_{i} = \frac{1}{h_{i} \pi D_{i}} + R_{f, i}$$ For the outer surface: $$R_{o} = \frac{1}{h_{o} \pi D_{o}} + R_{f, o}$$
03

Determine the total thermal resistance per unit length

We will add up all the resistances: $$R_{tot} = R_{i} + R_{t} + R_{o}$$
04

Calculate the overall heat transfer coefficients based on inner and outer surface areas

We can find the overall heat transfer coefficients, \(U_i\) and \(U_o\), based on the inner and outer surface areas: For the inner surface: $$U_{i} = \frac{1}{R_{tot}} \pi D_{i}$$ For the outer surface: $$U_{o} = \frac{1}{R_{tot}} \pi D_{o}$$ Now we can plug in the given values and perform the calculations to obtain the thermal resistance of the heat exchanger per unit length \((R_{tot})\), and the overall heat transfer coefficients \((U_i\) and \(U_o)\).

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Most popular questions from this chapter

A shell-and-tube heat exchanger with 2-shell passes and 8 -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 side at \(95^{\circ} \mathrm{C}\) and leaves at \(45^{\circ} \mathrm{C}\). If the overall heat transfer coefficient is \(950 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), determine the heat transfer surface area of the heat exchanger.

Steam is to be condensed on the shell side of a 2-shell-passes and 8-tube- passes condenser, with 20 tubes in each pass. Cooling water enters the tubes a rate of \(2 \mathrm{~kg} / \mathrm{s}\). If the heat transfer area is \(14 \mathrm{~m}^{2}\) and the overall heat transfer coefficient is \(1800 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), the effectiveness of this condenser is (a) \(0.70\) (b) \(0.80\) (c) \(0.90\) (d) \(0.95\) (e) \(1.0\)

By taking the limit as \(\Delta T_{2} \rightarrow \Delta T_{1}\), show that when \(\Delta T_{1}=\Delta T_{2}\) for a heat exchanger, the \(\Delta T_{\mathrm{lm}}\) relation reduces to \(\Delta T_{\mathrm{lm}}=\Delta T_{1}=\Delta T_{2} .\)

A shell-and-tube heat exchanger is used for cooling \(47 \mathrm{~kg} / \mathrm{s}\) of a process stream flowing through the tubes from \(160^{\circ} \mathrm{C}\) to \(100^{\circ} \mathrm{C}\). This heat exchanger has a total of 100 identical tubes, each with an inside diameter of \(2.5 \mathrm{~cm}\) and negligible wall thickness. The average properties of the process stream are: \(\rho=950 \mathrm{~kg} / \mathrm{m}^{3}, k=0.50 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, c_{p}=3.5 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\) and \(\mu=2.0 \mathrm{mPa} \cdot \mathrm{s}\). The coolant stream is water \(\left(c_{p}=4.18 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\) at a flow rate of \(66 \mathrm{~kg} / \mathrm{s}\) and an inlet temperature of \(10^{\circ} \mathrm{C}\), which yields an average shell-side heat transfer coefficient of \(4.0 \mathrm{~kW} / \mathrm{m}^{2} \cdot \mathrm{K}\). Calculate the tube length if the heat exchanger has \((a)\) a 1 -shell pass and a 1 -tube pass and (b) a 1-shell pass and 4-tube passes.

Write an essay on the static and dynamic types of regenerative heat exchangers and compile information about the manufacturers of such heat exchangers. Choose a few models by different manufacturers and compare their costs and performance.

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