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

Liquid water flows in a circular tube at a mass flow rate of $0.12 \mathrm{~kg} / \mathrm{s}\(. The water enters the tube at \)65^{\circ} \mathrm{C}\(, where it is heated at a rate of \)5.5 \mathrm{~kW}$. The tube is circular with a length of \(3 \mathrm{~m}\) and an inner diameter of $25 \mathrm{~mm}$. The tube surface is maintained isothermal. The inner surface of the tube is lined with polyvinylidene chloride (PVDC) lining. The recommended maximum temperature for PVDC lining is \(79^{\circ} \mathrm{C}\) (ASME Code for Process Piping, ASME B31.3-2014, Table A323.4.3). Is the PVDC lining suitable for the tube under these conditions? Evaluate the fluid properties at \(70^{\circ} \mathrm{C}\). Is this an appropriate temperature at which to evaluate the fluid properties?

Short Answer

Expert verified
Provide a brief explanation for your answer.

Step by step solution

01

Calculate the final temperature of water exiting the tube

To find the final temperature, we can use the energy balance equation: \(q = m \cdot C_p \cdot \Delta T\), where \(q\) is the heat input rate, \(m\) is the mass flow rate of water, \(C_p\) is the specific heat capacity of water, and \(\Delta T\) is the change in temperature. We are given \(q = 5.5 \mathrm{~kW}\) and \(m = 0.12 \mathrm{~kg} / \mathrm{s}\). The specific heat capacity of water at \(70^{\circ} \mathrm{C}\) can be taken as \(C_p = 4.18 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\). We can rearrange the energy balance equation to find \(\Delta T\): \(\Delta T = \frac{q}{m \cdot C_p}\)
02

Calculate the change in temperature and the final temperature

Now, we can plug the given values into our formula: \(\Delta T = \frac{5.5 \mathrm{~kW}}{0.12 \mathrm{~kg} / \mathrm{s} \cdot 4.18 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}} = 10.85 ^{\circ} \mathrm{C}\) The initial temperature of the water is \(65^{\circ}\mathrm{C}\). Therefore, the final temperature of water exiting the tube is: \(T_{final} = T_{initial} + \Delta T = 65^{\circ}\mathrm{C} + 10.85^{\circ}\mathrm{C} = 75.85^{\circ}\mathrm{C}\)
03

Compare the final temperature with the maximum allowable temperature for PVDC lining

The maximum allowable temperature for PVDC lining is \(79^{\circ}\mathrm{C}\). Since the final temperature of water is lower than the maximum allowable temperature for PVDC lining (\(75.85^{\circ}\mathrm{C} < 79^{\circ}\mathrm{C}\)), the PVDC lining is suitable for the tube under these conditions.
04

Discuss the appropriateness of evaluating the fluid properties at \(70^{\circ}\mathrm{C}\)

We evaluated the fluid properties at \(70^{\circ}\mathrm{C}\), which is an average temperature between the initial temperature and the final temperature of the water. This is an appropriate temperature for evaluating the fluid properties, as it provides an estimation of the fluid properties during the heating process when the temperature changes between the initial and final values. This estimate should provide reasonably accurate results for this problem.

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

Glycerin is being heated by flowing between two very thin parallel 1 -m-wide and \(10-\mathrm{m}\)-long plates with \(12.5\)-mm spacing. The glycerin enters the parallel plates with a temperature \(20^{\circ} \mathrm{C}\) and a mass flow rate of \(0.7 \mathrm{~kg} / \mathrm{s}\). The outer surface of the parallel plates is subjected to hydrogen gas (an ideal gas at \(1 \mathrm{~atm}\) ) flow width-wise in parallel over the upper and lower surfaces of the two plates. The free-stream hydrogen gas has a velocity of \(3 \mathrm{~m} / \mathrm{s}\) and a temperature of \(150^{\circ} \mathrm{C}\). Determine the outlet mean temperature of the glycerin, the surface temperature of the parallel plates, and the total rate of heat transfer. Evaluate the properties for glycerin at \(30^{\circ} \mathrm{C}\) and the properties of \(\mathrm{H}_{2}\) gas at \(100^{\circ} \mathrm{C}\). Are these good assumptions?

Water enters a 2-cm-diameter and 3-m-long tube whose walls are maintained at \(100^{\circ} \mathrm{C}\) with a bulk temperature of \(25^{\circ} \mathrm{C}\) and a volume flow rate of \(3 \mathrm{~m}^{3} / \mathrm{h}\). Neglecting the entrance effects and assuming turbulent flow, the Nusselt number can be determined from \(\mathrm{Nu}=0.023 \mathrm{Re}^{0.8} \mathrm{Pr}^{0.4}\). The convection heat transfer coefficient in this case is (a) \(4140 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (b) \(6160 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (c) \(8180 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (d) \(9410 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (e) \(2870 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (For water, use $k=0.610 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \operatorname{Pr}=6.0, \mu=9.0 \times\( \)10^{-4} \mathrm{~kg} / \mathrm{m} \cdot \mathrm{s}, \rho=1000 \mathrm{~kg} / \mathrm{m}^{3}$.)

In fully developed laminar flow inside a circular pipe, the velocities at \(r=0.5 R\) (midway between the wall surface and the centerline) are measured to be 3,6 , and \(9 \mathrm{~m} / \mathrm{s}\). (a) Determine the maximum velocity for each of the measured midway velocities. (b) By varying \(r / R\) for $-1 \leq r / R \leq 1$, plot the velocity profile for each of the measured midway velocities with \(r / R\) as the \(y\)-axis and \(V(r / R)\) as the \(x\)-axis.

In a heating system, liquid water flows in a circular tube at a mass flow rate of \(3.5 \mathrm{~g} / \mathrm{s}\). The water enters the tube at $5^{\circ} \mathrm{C}\(, where it is heated at a rate of \)1 \mathrm{~kW}$. The tube surface is maintained at a constant temperature. The effectiveness of the system to heat water in the tube has been determined to have a number of transfer units of \(\mathrm{NTU}=2\). According to the service restrictions of the ASME Boiler and Pressure Vessel Code (ASME BPVC.IV-2015, HG-101), hot water heaters should not be operating at temperatures exceeding $120^{\circ} \mathrm{C}$ at or near the heater outlet. The inner surface of the tube is lined with polyvinylidene chloride (PVDC) lining. According to the ASME Code for Process Piping (ASME B31.3-2014, Table A323.4.3), the recommended maximum temperature for PVDC lining is \(79^{\circ} \mathrm{C}\). To comply with both ASME codes, determine \((a)\) Whether the water exiting the tube is at a temperature below \(120^{\circ} \mathrm{C}\). (b) Whether the inner surface temperature of the tube exceeds \(79^{\circ} \mathrm{C}\). Evaluate the fluid properties at \(40^{\circ} \mathrm{C}\). Is this an appropriate temperature to evaluate the fluid properties?

A 4-m-long tube is subjected to uniform wall heat flux. The tube has an inside diameter of \(0.0149 \mathrm{~m}\) and a flow rate of $7.8 \times 10^{-5} \mathrm{~m}^{3} / \mathrm{s}$. The liquid flowing inside the tube is an ethylene glycol-distilled water mixture with a mass fraction of \(0.5\). Determine the apparent (developing) friction factor at the location \(x / D=20\) if the inlet configuration of the tube is: \((a)\) re-entrant and \((b)\) square- edged. At this location, the local Grashof number is Gr \(=24,000\), and the properties of the mixture of distilled water and ethylene glycol are: \(\operatorname{Pr}=20.9\), $\nu=2.33 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\(, and \)\mu_{y} / \mu_{s}=1.25$.

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