Warning: foreach() argument must be of type array|object, bool given in /var/www/html/web/app/themes/studypress-core-theme/template-parts/header/mobile-offcanvas.php on line 20

In a one-shell and two-tube heat exchanger, cold water with inlet temperature of \(20^{\circ} \mathrm{C}\) is heated by hot water supplied at the inlet at \(80^{\circ} \mathrm{C}\). The cold and hot water flow rates are $5000 \mathrm{~kg} / \mathrm{h}\( and \)10,000 \mathrm{~kg} / \mathrm{h}$, respectively. If the shell-andtube heat exchanger has a \(U A_{s}\) value of \(11,600 \mathrm{~W} / \mathrm{K}\), determine the cold water and hot water outlet temperatures. Assume $c_{p c}=4178 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\( and \)c_{p t}=4188 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}$.

Short Answer

Expert verified
Based on the given data and calculations, the cold water outlet temperature in the one-shell and two-tube heat exchanger is 53.33°C, and the hot water outlet temperature is 64.67°C.

Step by step solution

01

Calculate the heat capacities of cold and hot streams

Calculate the heat capacities for both cold and hot streams using their mass flow rates and specific heats: For the cold stream: \(m_c c_{p c} = 5000 \frac{\text{kg}}{\text{h}} * 4178 \frac{\text{J}}{\text{kg} \cdot \text{K}} = 20,890,000 \frac{\text{J}}{\text{h} \cdot \text{K}}\) For the hot stream: \(m_t c_{p t} = 10000 \frac{\text{kg}}{\text{h}} * 4188 \frac{\text{J}}{\text{kg} \cdot \text{K}} = 41,880,000 \frac{\text{J}}{\text{h} \cdot \text{K}}\)
02

Determine the Maximum Possible Heat Transfer Rate

Choose the minimum value of heat capacities and the maximum value of temperature difference: Minimum heat capacity: min(20,890,000 ; 41,880,000) = 20,890,000 J/(h·K) Maximum temperature difference: ΔT = |80 - 20| = 60 K Maximum Possible Heat Transfer Rate = (Minimum heat capacity) * (Maximum temperature difference) = 20,890,000 J/(h·K) * 60 K = 1,253,400,000 J/h
03

Calculate the Heat Transfer Rate

Given the heat exchanger UA_s value of 11,600 W/K, we can calculate the heat transfer rate as follows: Effectiveness = \(\frac{Q}{Q_{\text{max}}}\) Rearranging the formula for Q, we find Q = Effectiveness * Q_max (where Q_max = 1,253,400,000 J/h) Next, we find the effectiveness of the heat exchanger using the given UA_s value: Effectiveness = \(\frac{\text{UA}_s}{\text{min}(m_c c_{p c},m_t c_{p t})}\) Effectiveness = \(\frac{11,600\frac{\text{W}}{\text{K}}}{20,890,000\frac{\text{J}}{\text{h} \cdot \text{K}}}\) = 0.55509 (unitless) Now we can calculate the heat transfer rate Q: Q = 0.55509 * 1,253,400,000 J/h = 696,373,237 J/h
04

Determine the Cold and Hot Water Outlet Temperatures

Now we have the required heat transfer rate Q, and we can determine the outlet temperatures for the hot and cold streams. For the cold stream: \(Q = m_c c_{p c} (T_{c \text{ out}} - T_{c \text{ in}})\) Rearranging to solve for \(T_{c \text{ out}}\): \(T_{c \text{ out}} = T_{c \text{ in}} + \frac{Q}{m_c c_{p c}} = 20^{\circ}\mathrm{C} + \frac{696,373,237\frac{\text{J}}{\text{h}}}{20,890,000\frac{\text{J}}{\text{h} \cdot \text{K}}}\) \(T_{c \text{ out}} = 53.33^{\circ}\mathrm{C}\) For the hot stream: \(Q = m_t c_{p t} (T_{t \text{ in}} - T_{t \text{ out}})\) Rearranging to solve for \(T_{t \text{ out}}\): \(T_{t \text{ out}} = T_{t \text{ in}} - \frac{Q}{m_t c_{p t}} = 80^{\circ}\mathrm{C} - \frac{696,373,237\frac{\text{J}}{\text{h}}}{41,880,000\frac{\text{J}}{\text{h} \cdot \text{K}}}\) \(T_{t \text{ out}} = 64.67^{\circ}\mathrm{C}\) Thus, the cold water outlet temperature is \(53.33^{\circ}\mathrm{C}\), and the hot water outlet temperature is \(64.67^{\circ}\mathrm{C}\).

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with Vaia!

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

Ethanol is vaporized at $78^{\circ} \mathrm{C}\left(h_{f \mathrm{~g}}=846 \mathrm{~kJ} / \mathrm{kg}\right)$ in a double-pipe parallel-flow heat exchanger at a rate of \(0.04 \mathrm{~kg} / \mathrm{s}\) by hot oil \(\left(c_{p}=2200 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) that enters at \(115^{\circ} \mathrm{C}\). If the heat transfer surface area and the overall heat transfer coefficients are \(6.2 \mathrm{~m}^{2}\) and $320 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, respectively, determine the outlet temperature and the mass flow rate of oil using \((a)\) the LMTD method and \((b)\) the \(\varepsilon-\mathrm{NTU}\) method.

Hot water coming from the engine is to be cooled by ambient air in a car radiator. The aluminum tubes in which the water flows have a diameter of $4 \mathrm{~cm}$ and negligible thickness. Fins are attached on the outer surface of the tubes in order to increase the heat transfer surface area on the air side. The heat transfer coefficients on the inner and outer surfaces are 2000 and \(150 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), respectively. If the effective surface area on the finned side is 12 times the inner surface area, the overall heat transfer coefficient of this heat exchanger based on the inner surface area is (a) \(760 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (b) \(832 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (c) \(947 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (d) \(1075 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (e) \(1210 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\)

Water \(\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) enters the \(2.5\)-cm-internaldiameter tube of a double-pipe counterflow heat exchanger at \(20^{\circ} \mathrm{C}\) at a rate of $2.2 \mathrm{~kg} / \mathrm{s}\(. Water is heated by steam condensing at \)120^{\circ} \mathrm{C}\left(h_{f g}=2203 \mathrm{~kJ} / \mathrm{kg}\right)$ in the shell. If the overall heat transfer coefficient of the heat exchanger is $700 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, determine the length of the tube required in order to heat the water to \(80^{\circ} \mathrm{C}\) using \((a)\) the LMTD method and \((b)\) the \(\varepsilon-\mathrm{NTU}\) method.

In a textile manufacturing plant, the waste dyeing water $\left(c_{p}=4295 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( at \)80^{\circ} \mathrm{C}$ is to be used to preheat fresh water $\left(c_{p}=4180 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\( at \)10^{\circ} \mathrm{C}$ at the same flow rate in a double-pipe counterflow heat exchanger. The heat transfer surface area of the heat exchanger is \(1.65 \mathrm{~m}^{2}\), and the overall heat transfer coefficient is $625 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. If the rate of heat transfer in the heat exchanger is \)35 \mathrm{~kW}$, determine the outlet temperature and the mass flow rate of each fluid stream.

What are the common causes of fouling in a heat exchanger? How does fouling affect heat transfer and pressure drop?

See all solutions

Recommended explanations on Physics Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.

Sign-up for free