Fundamentals of Heat and Mass Transfer
Fundamentals of Heat and Mass Transfer
7th Edition
ISBN: 9780470501979
Author: Frank P. Incropera, David P. DeWitt, Theodore L. Bergman, Adrienne S. Lavine
Publisher: Wiley, John & Sons, Incorporated
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Chapter 5, Problem 5.5P

For each of the following cases, determine an appropriate characteristic length L c and the corresponding Biot number Bi that is associated with the transient thermal response of the solid object. State whether the lumped capacitance approximation is valid. If temperature information is not provided. evaluate properties at T = 300 K .

  1. A toroidal shape of diameter D = 50 mm and cross-sectional area A c = 5 mm 2 is of thermal conductivity k = 2.3 W/m K . The surface of the torus is exposed to a coolant corresponding to a convection coefficient of h = 50 W/m 2 K .
  2. A long, hot AISI 304 stainless steel bar of rectangular cross section has dimensions w = 3 mm, W = 5 mm, and L = 100 mm . The bar is subjected to a coolant that provides a heat transfer coefficient of h = 15 W/m 2 K at all exposed surfaces.
  3. A long extruded aluminum (Alloy 2024) tube of inner and outer dimensions w = 20 mm and W = 24 mm, respectively, is suddenly submerged in water, resulting in a convection coefficient of h = 37 W/m 2 K at the four exterior tube surfaces. The tube is plugged at both ends. trapping stagnant air inside the tube.
  4. An L = 300 -mm -long solid stainless steel rod of diameter D = 13 mm and mass M = 0.328 kg is exposed to a convection coefficient of h = 30 W/m 2 K .
  5. A solid sphere of diameter D = 12 mm and thermal conductivity k = 120 W/m K is suspended in a large vacuum oven with internal wall temperatures of T sur = 20 ° C . The initial sphere temperature is T i = 100 ° C, and its emissivity is ε = 0.73.
  6. A long cylindrical rod of diameter D = 20 mm, density ρ = 2300 kg/m 3 , specific heat c p = 1750 J/kg K, and thermal conductivity k = 16 W/m K is suddenly exposed to convective conditions with T = 20 ° C . The rod is initially at a uniform temperature of T i = 200 ° C and reaches a spatially averaged temperature of T = 100 ° C at t = 225 s .
  7. Repeat part (f) but now consider a rod diameter of D = 200 mm .

Chapter 5, Problem 5.5P, For each of the following cases, determine an appropriate characteristic length Lc and the , example  1Chapter 5, Problem 5.5P, For each of the following cases, determine an appropriate characteristic length Lc and the , example  2

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To maximize production and minimize pumping costs, crude oil is heated to reduce its viscosity during transportation from a production field. (1) Consider a pipe-in-pipe configuration consisting of concentric steel tubes with an intervening insulating material. The inner tube is used to transport warm crude oil through cold ocean water. The inner steel pipe ( ks = 40 W/m·K) has an inside diameter of Di,1 = 150 mm and wall thickness ti = 20 mm while the outer steel pipe has an inside diameter of Di,1 = 250 mm and wall thickness . Determine the maximum allowable crude oil temperature to ensure the polyurethane foam insulation ( kp = 0.0425 W/m·K) provides an external convection heat transfer coefficient of ho = 500 W/m2·K. The convection coefficient associated with the flowing crude oil is hi = 450 W/m2·K. (2) It is proposed to enhance the performance of the pipe-in-pipe device by replacing a thin ( ta =10 mm) section of polyurethane located at the outside of the inner pipe with an…
To maximize production and minimize pumping costs, crude oil is heated to reduce its viscosity during transportation from a production field. (1) Consider a pipe-in-pipe configuration consisting of concentric steel tubes with an intervening insulating material. The inner tube is used to transport warm crude oil through cold ocean water. The inner steel pipe (ks= 40 W/m·K) has an inside diameter of  Di, 1= 150 mm and wall thickness ti= 20 mm while the outer steel pipe has an inside diameter of  Di, 2= 250 mm and wall thickness to=ti. Determine the maximum allowable crude oil temperature to ensure the polyurethane foam insulation (kp= 0.0675 W/m·K) between the two pipes does not exceed its maximum service temperature of  Tp, max= 70°C. The ocean water is at ∞ T∞, o= -5°C and provides an external convection heat transfer coefficient of ho= 500 W/m2·K. The convection coefficient associated with the flowing crude oil is hi= 450 W/m2·K. (2) It is proposed to enhance the performance of the…

Chapter 5 Solutions

Fundamentals of Heat and Mass Transfer

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