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

Hot liquid is flowing in a steel pipe with an inner diameter of $D_{1}=22 \mathrm{~mm}\( and an outer diameter of \)D_{2}=27 \mathrm{~mm}$. The inner surface of the pipe is coated with a thin fluorinated ethylene propylene (FEP) lining. The thermal conductivity of the pipe wall is $15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. The pipe outer surface is subjected to a uniform flux of \(1200 \mathrm{~W} / \mathrm{m}^{2}\) for a length of \(1 \mathrm{~m}\). The hot liquid flowing inside the pipe has a mean temperature of $180^{\circ} \mathrm{C}\( and a convection heat transfer coefficient of \)50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. The interface between the FEP lining and the steel surface has a thermal contact conductance of $1500 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Determine the temperatures at the lining and at the pipe outer surface for the pipe length subjected to the uniform heat flux. What is the total thermal resistance between the two temperatures? The ASME Code for Process Piping (ASME B31.3-2014, A.323) recommends a maximum temperature for FEP lining to be \(204^{\circ} \mathrm{C}\). Does the FEP lining comply with the recommendation of the code?

Short Answer

Expert verified
Question: Determine the temperatures at the lining and the pipe outer surface, and check if the FEP lining complies with the ASME Code for Process Piping, given the heat transfer rate through the wall, the thermal resistance of the steel wall, FEP lining-steel interface, and convection at the pipe inner surface.

Step by step solution

01

Calculate the heat transfer rate

We are given that the pipe outer surface is subjected to a uniform flux of \(1200\mathrm{~W/m^2}\). To find the total heat transfer rate (\(\dot{Q}\)) through the wall, we multiply the flux by the surface area (assuming a length of 1m, and using the outer diameter): $$\dot{Q} = 1200 \frac{\text{W}}{\text{m}^2} \cdot \pi D_2 \times 1\text{m}$$
02

Calculate the thermal resistance of the steel wall

The thermal resistance of the steel wall (\(R_{steel}\)) can be found using the formula: $$R_{steel} = \frac{D_2 - D_1}{2 \pi \lambda_\text{steel} L}$$ where \(\lambda_\text{steel}\) is the thermal conductivity of the steel (15 W/mK) and \(L\) is the length of the pipe (1m).
03

Calculate the thermal resistance of the FEP lining-steel interface

The thermal resistance of the FEP lining-steel interface (\(R_\text{fep-steel}\)) can be found using the formula: $$R_\text{fep-steel} = \frac{1}{h_\text{fep-steel} A}$$ where \(h_\text{fep-steel}\) is the thermal contact conductance (1500 W/m²K) and \(A\) is the surface area of the interface (using the inner diameter, and assuming a length of 1m): $$A = \pi D_1 \times 1\text{m}$$
04

Calculate the thermal resistance of the convection at the pipe inner surface

The thermal resistance of the convection at the pipe inner surface (\(R_\text{convection}\)) can be found using the formula: $$R_\text{convection} = \frac{1}{h_\text{convection} A}$$ where \(h_\text{convection}\) is the convection heat transfer coefficient (50 W/m²K).
05

Calculate the total thermal resistance

The total thermal resistance (\(R_\text{total}\)) is the sum of the three resistances calculated in steps 2-4: $$R_\text{total} = R_{steel} + R_\text{fep-steel} + R_\text{convection}$$
06

Calculate the temperatures at the lining and the pipe outer surface

To find the temperature at the lining (\(T_\text{lining}\)), we add the product of the heat transfer rate and the thermal resistance of the FEP lining-steel interface to the temperature of the hot liquid: $$T_\text{lining} = T_\text{liquid} + \dot{Q} R_\text{fep-steel}$$ To find the temperature at the pipe outer surface (\(T_\text{outer}\)), we add the product of the heat transfer rate and the total thermal resistance to the temperature of the hot liquid: $$T_\text{outer} = T_\text{liquid} + \dot{Q} R_\text{total}$$
07

Check if the FEP lining complies with the Code

To check if the FEP lining complies with the ASME Code for Process Piping, we compare the temperature at the lining with the maximum temperature recommended for FEP lining (\(204^{\circ}\text{C}\)). If the temperature at the lining is less than or equal to the maximum recommended temperature, the FEP lining complies with the Code. After calculating the temperatures and comparing them to the given limits, we will have a complete solution to the 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

A \(3-\mathrm{cm}\)-long, \(2-\mathrm{mm} \times 2-\mathrm{mm}\) rectangular cross-section aluminum fin \((k=237 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) is attached to a surface. If the fin efficiency is 65 percent, the effectiveness of this single fin is (a) 39 (b) 30 (c) 24 (d) 18 (e) 7

Hot air is to be cooled as it is forced to flow through the tubes exposed to atmospheric air. Fins are to be added in order to enhance heat transfer. Would you recommend attaching the fins inside or outside the tubes? Why? When would you recommend attaching fins both inside and outside the tubes?

A row of 3 -ft-long and 1-in-diameter used uranium fuel rods that are still radioactive are buried in the ground parallel to each other with a center-to- center distance of 8 in at a depth of \(15 \mathrm{ft}\) from the ground surface at a location where the thermal conductivity of the soil is $0.6 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft} \cdot{ }^{\circ} \mathrm{F}$. If the surface temperatures of the rods and the ground are \(350^{\circ} \mathrm{F}\) and \(60^{\circ} \mathrm{F}\), respectively, determine the rate of heat transfer from the fuel rods to the atmosphere through the soil.

A 0.6-m-diameter, 1.9-m-long cylindrical tank containing liquefied natural gas (LNG) at \(-160^{\circ} \mathrm{C}\) is placed at the center of a \(1.9\)-m-long \(1.4-\mathrm{m} \times 1.4-\mathrm{m}\) square solid bar made of an insulating material with \(k=0.0002 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). If the outer surface temperature of the bar is \(12^{\circ} \mathrm{C}\), determine the rate of heat transfer to the tank. Also, determine the LNG temperature after one month. Take the density and the specific heat of LNG to be $425 \mathrm{~kg} / \mathrm{m}^{3}\( and \)3.475 \mathrm{~kJ} / \mathrm{kg} \cdot{ }^{\circ} \mathrm{C}$, respectively.

Steam in a heating system flows through tubes whose outer diameter is $3 \mathrm{~cm}\( and whose walls are maintained at a temperature of \)120^{\circ} \mathrm{C}\(. Circular aluminum alloy fins \)(k=180 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\( of outer diameter \)6 \mathrm{~cm}$ and constant thickness \(t=2 \mathrm{~mm}\) are attached to the tube, as shown in Fig. P3-201. The space between the fins is \(3 \mathrm{~mm}\), and thus there are 200 fins per meter length of the tube. Heat is transferred to the surrounding air at \(25^{\circ} \mathrm{C}\), with a combined heat transfer coefficient of $60 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Determine the increase in heat transfer from the tube per meter of its length as a result of adding fins.

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