14 Pages

Heat Chap15-055

Course: AET AET432, Spring 2007
School: ASU
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15 Chapter Cooling of Electronic Equipment 15-55 A plastic DIP with 16 leads is cooled by forced air. Using data supplied by the manufacturer, the junction temperature is to be determined. Assumptions Steady operating conditions exist. Analysis The junction-to-ambient thermal resistance of the device with 16 leads corresponding to an air velocity of 300 m/min is determined from Fig.15-23 to be R junction ambient...

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15 Chapter Cooling of Electronic Equipment 15-55 A plastic DIP with 16 leads is cooled by forced air. Using data supplied by the manufacturer, the junction temperature is to be determined. Assumptions Steady operating conditions exist. Analysis The junction-to-ambient thermal resistance of the device with 16 leads corresponding to an air velocity of 300 m/min is determined from Fig.15-23 to be R junction ambient Air 25 C 300 m/min 50 C / W 2W Then the junction temperature becomes Q T junction T junction Tambient R junction Tambient ambient QR junction ambient 25 C + (2 W)(50 C/W) = 125 C When the fan fails the total thermal resistance is determined from Fig.15-23 by reading the value for zero air velocity (the intersection point of the curve with the vertical axis) to be R junction ambient 70 C / W which yields Q T junction T junction Tambient R junction Tambient ambient QR junction ambient 25 C + (2 W)(70 C/W) = 165 C 15-56 A PCB with copper cladding is given. The percentages of heat conduction along the copper and epoxy layers as well as the effective thermal conductivity of the PCB are to be determined. Assumptions 1 Steady operating conditions exist. 2 Heat conduction along the PCB is one-dimensional since heat transfer from side surfaces is negligible. 3 The thermal properties of epoxy and copper layers are constant. Analysis Heat conduction along a layer is proportional to the thermal conductivity-thickness product (kt) which is determined for each layer and the entire PCB to be ( kt ) copper ( kt ) epoxy ( kt ) PCB (386 W / m. C)(0.06 10 m) (0.26 W / m. C)(0.5 10-3 m) ( kt ) copper ( kt ) epoxy -3 PCB 12 cm 12 cm 0.02316 W/ C 0.00013 W/ C 0.02329 W/ C Q 0.02316 0.00013 Therefore the percentages of heat conduction along the epoxy board are f epoxy (kt) epoxy (kt) PCB 0.00013 W/ C 0.02316 W/ C 0.0056 0.6% Copper t = 0.06 mm Epoxy t = 0.5 mm and fcopper (100 0.6)% 99.4% Then the effective thermal conductivity becomes k eff (kt) epoxy t epoxy (kt) copper t copper (0.02316 0.00013) W/ C (0.06 + 0.5) 10 -3 m 41.6 W/m. C 15-16 Chapter 15 Cooling of Electronic Equipment 15-57 "!PROBLEM 15-057" "GIVEN" length=0.12 "[m]" width=0.12 "[m]" "t_copper=0.06 [mm], parameter to be varied" t_epoxy=0.5 "[mm]" k_copper=386 "[W/m-C]" k_epoxy=0.26 "[W/m-C]" "ANALYSIS" kt_copper=k_copper*t_copper*Convert(mm, m) kt_epoxy=k_epoxy*t_epoxy*Convert(mm, m) kt_PCB=kt_copper+kt_epoxy f_copper=kt_copper/kt_PCB*Convert(, %) f_epoxy=100-f_copper k_eff=(kt_epoxy+kt_copper)/((t_epoxy+t_copper)*Convert(mm, m)) Tcopper [mm] 0.02 0.025 0.03 0.035 0.04 0.045 0.05 0.055 0.06 0.065 0.07 0.075 0.08 0.085 0.09 0.095 0.1 fcopper [%] 98.34 98.67 98.89 99.05 99.17 99.26 99.33 99.39 99.44 99.48 99.52 99.55 99.58 99.61 99.63 99.65 99.66 keff [W/m-C] 15.1 18.63 22.09 25.5 28.83 32.11 35.33 38.49 41.59 44.64 47.63 50.57 53.47 56.31 59.1 61.85 64.55 15-17 Chapter 15 Cooling of Electronic Equipment 15-18 Chapter 15 Cooling of Electronic Equipment 15-58 The heat generated in a silicon chip is conducted to a ceramic substrate to which it is attached. The Q temperature difference between the front and back surfaces of the chip is to be determined. Assumptions 1 Steady operating conditions exist. 2 Heat conduction along the chip is onedimensional. Analysis The thermal resistance of silicon chip is Rchip L kA 0.5 10-3 m (130 W / m. C)(0.006 0.006)m2 6 6 3W Chip 0.5 mm 01068 C / W . Ceramic substrate Then the temperature difference across the chip becomes T QRchip (3 W)(0.1068 C/W) = 0.32 C 15-59E The dimensions of an epoxy glass laminate are given. The thermal resistances for heat flow along the layers and across the thickness are to be determined. Assumptions 1 Heat conduction in the laminate is one-dimensional in either case. 2 Thermal properties of the laminate are constant. Analysis The thermal resistances of the PCB along the 7 in long side and across its thickness are Ralong length Qlength 6 in 7 in Qthickness L kA (7/12) ft (0.15 Btu/h.ft. F)(6/12 ft)(0.05/12 ft) 1867 h. F/Btu (a) Racross (b) thickness L kA (0.05/12) ft (0.15 Btu/h.ft. F)(7/12 ft)(6/12 ft) 0.095 h. F/Btu 0.05 in 15-19 Chapter 15 Cooling of Electronic Equipment 15-60 Cylindrical copper fillings are planted throughout an epoxy glass board. The thermal resistance of the board across its thickness is to be determined. Assumptions 1 Heat conduction along the board is one-dimensional. 2 Thermal properties of the board are constant. Analysis The number of copper fillings on the board is n Area of board Area of one square (150 mm)(180 mm) (3 mm)(3 mm) 3 mm Copper filing 1 mm 3 mm Epoxy board 3000 The surface areas of the copper fillings and the remaining part of the epoxy layer are Acopper Atotal Aepoxy D2 (0.001 m) 2 (3000) 0.002356 m2 4 4 (length)( width) (015 m)(0.18 m) = 0.027 m2 . n Atotal Acopper 0.027 0.002356 0.024644 m2 The thermal resistance of each material is Rcopper Repoxy L kA L kA 0.0014 m (386 W / m. C)(0.002356 m2 ) 0.0014 m (0.26 W / m. C)(0.024644 m2 ) 0.00154 C / W 0.2185 C / W Since these two resistances are in parallel, the equivalent thermal resistance of the entire board is 1 Rboard 1 Repoxy 1 Rcopper 1 0.2185 C/W 1 0.00154 C/W Rboard 0.00153 C/W 15-20 Chapter 15 Cooling of Electronic Equipment 15-61 "!PROBLEM 15-061" "GIVEN" length=0.18 "[m]" width=0.15 "[m]" k_epoxy=0.26 "[W/m-C]" t_board=1.4/1000 "[m]" k_filling=386 "[W/m-C], parameter to be varied" "D_filling=1 [mm], parameter to be varied" s=3/1000 "[m]" "ANALYSIS" A_board=length*width n_filling=A_board/s^2 A_filling=n_filling*pi*(D_filling*Convert(mm, m))^2/4 A_epoxy=A_board-A_filling R_filling=t_board/(k_filling*A_filling) R_epoxy=t_board/(k_epoxy*A_epoxy) 1/R_board=1/R_epoxy+1/R_filling kfilling [W/m-C] 10 29.5 49 68.5 88 107.5 127 146.5 166 185.5 205 224.5 244 263.5 283 302.5 322 341.5 361 380.5 400 Dfilling [mm] 0.5 0.6 0.7 0.8 0.9 1 1.1 1.2 1.3 1.4 1.5 Rboard [C/W] 0.04671 0.01844 0.01149 0.008343 0.00655 0.005391 0.00458 0.003982 0.003522 0.003157 0.00286 0.002615 0.002408 0.002232 0.00208 0.001947 0.00183 0.001726 0.001634 0.00155 0.001475 Rboard [C/W] 0.005977 0.004189 0.003095 0.002378 0.001884 0.001529 0.001265 0.001064 0.0009073 0.0007828 0.0006823 15-21 Chapter 15 Cooling of Electronic Equipment 1.6 1.7 1.8 1.9 2 0.0005999 0.0005316 0.0004743 0.0004258 0.0003843 15-22 Chapter 15 Cooling of Electronic Equipment 15-62 A circuit board with uniform heat generation is to be conduction cooled by a copper heat frame. Temperature distribution along the heat PCB frame and the maximum temperature in the PCB are to be determined. 15 cm 18 cm Assumptions 1 Steady operating conditions exist 2 Thermal properties are constant. 3 There is no direct heat dissipation from the surface of the PCB, and thus all the heat generated is conducted by the heat frame to the heat sink. Heat frame Epoxy Analysis The properties and dimensions of adhesive Cold plate various section of the PCB are summarized below as Section and material Thermal Thickness Heat transfer surface conductivity area Epoxy board 2 mm 0.26 W/m. C 10 mm 120 mm Epoxy adhesive 0.12 mm 1.8 W/m. C 10 mm 120 mm Copper heat frame 1.5 mm 386 W/m. C 10 mm 120 mm (normal to frame) Copper heat frame 10 mm 386 W/m. C 15 mm 120 mm (along the frame) Using the values in the table, the various thermal resistances are determined to be L 0.002 m Repoxy 6.41 C / W kA (0.26 W / m. C)(0.01 m 012 m) . L 0.00012 m Radhesive 0.056 C / W kA (1.8 W / m. C)(0.01 m 0.12 m) L 0.0015 m Rcopper , 0.0032 C / W kA (386 W / m. C)(0.01 m 0.12 m) L 0.01 m R frame Rcopper , parallel 0144 C / W . kA (386 W / m. C)(0.0015 0.12 m) The combined resistance between the electronic components on each strip and the heat frame can be determined by adding the three thermal resistances in series to be Rvertical Repoxy Radhesive Rcopper, 6.41 0.056 0.0032 6.469 C / W The temperatures along the heat frame can be determined from the relation T1 T2 T3 T4 T5 T6 T7 T8 T0 T1 T2 Q1 0 R1 Q2 1 R2 Q R 3 2 0 1 T Thigh Tlow QR . Then, 30 C + (22.5 W)(0.144 C / W) = 33.24 C 33.24 C + (19.5 W)(0.144 C / W) = 36.05 C 36.05 C + (16.5 W)(0.144 C / W) = 38.42 C 38.42 C + (13.5 W)(0.144 C / W) = 40.36 C 40.36 C + (10.5 W)(0.144 C / W) = 41.87 C 4187 C + (7.5 W)(0.144 C / W) = 42.95 C . 42.95 C + (4.5 W)(0.144 C / W) = 43.60 C 4388 C + (1.5 W)(0.144 C / W) = 43.81 C . T9 3 2 3 4 T3 Q4 3 R4 T4 Q5 4 R5 T Q R 5 6 5 6 5 6 7 3W Repox y T6 T7 Q7 6 R7 Q8 7 R8 The maximum surface temperature on the PCB is Tmax T9 T8 Qvertical Rvertical 4381 C + (3 W)(6.469 C / W) = 63.2 C . 22.5 W T0 T1 19.5 W T2 16.5 W T3 13.5 W T4 10.5 W T5 7.5 W T6 4.5 W T7 1.5 W T8 Radhesive Rcopper 15-23 Chapter 15 Cooling of Electronic Equipment 15-63 A circuit board with uniform heat generation is to be conduction cooled by aluminum wires inserted into it. The magnitude and location of the maximum temperature in the PCB is to be determined. Assumptions 1 Steady conditions operating exist 2 Thermal properties are constant. 3 There is no direct heat dissipation from the surface of the PCB. Analysis The number of wires in the board is n 150 mm 2 mm 75 Double sided PCB 12 cm 15 cm Aluminum wire, D = 1 mm The surface areas of the aluminum wires and the remaining part of the epoxy layer are Aalu min um Atotal Aepoxy D (0.001 m) (75) 0.0000589 m2 4 4 (length)( width) (0.003 m)(0.15 m) = 0.00045 m2 n Atotal Aalu min um 0.00045 0.0000589 0.0003911 m2 2 2 2 mm Considering only half of the circuit board because of symmetry, the thermal resistance of each material per 1-cm length is determined to be Ralu min um Repoxy L kA L kA 0.01 m (237 W / m. C)(0.0000589 m 2 ) 0.01 m (0.26 W / m. C)(0.0003911 m 2 ) 0.716 C / W 98.34 C / W 3 mm Since these two resistances are in parallel, the equivalent thermal resistance per cm is determined from 1 Rboard 1 Repoxy 1 Ralu min um 1 0.716 C / W 1 98.34 C / W Rboard 0.711 C / W Maximum temperature occurs in the middle of the plate along the 20 cm length, which is determined to be Tmax Tend Tboard ,total Tend Qi Rboard ,1 cm Tend Rboard ,1 cm Qi 30 C + (0.711 C / W)(15 +13.5 +12 +10.5 + 9 + 7.5 + 6 + 4.5 + 3 +1.5)W = 88.7 C 15 W 13.5 W 12 W 10.5 W 9W 7.5 W 6W 4.5 W 3W 1.5 W 30 C 1 cm Tmax Rboard 15-24 Chapter 15 Cooling of Electronic Equipment 15-64 A circuit board with uniform heat generation is to be conduction cooled by copper wires inserted in it. The magnitude and location of the maximum temperature in the PCB is to be determined. Assumptions 1 Steady operating conditions exist 2 Thermal properties are constant. 3 There is no direct heat dissipation from the surface of the PCB. Analysis The number of wires in the circuit board is n 150 mm 2 mm 75 Double sided PCB 12 cm 15 cm Copper wire, D = 1 mm The surface areas of the copper wires and the remaining part of the epoxy layer are Acopper Atotal Aepoxy D2 (0.001 m) 2 n (75) 0.0000589 m2 4 4 (length)( width) (0.003 m)(0.15 m) = 0.00045 m2 Atotal Acopper 0.00045 0.0000589 0.0003911 m2 2 mm Considering only half of the circuit board because of symmetry, the thermal resistance of each material per 1-cm length is determined to be Rcopper Repoxy L kA L kA 0.01 m (386 W / m. C)(0.0000589 m2 ) 0.01 m (0.26 W / m. C)(0.0003911 m2 ) 0.440 C / W 98.34 C / W 3 mm Since these two resistances are in parallel, the equivalent thermal resistance is determined from 1 Rboard 1 Repoxy 1 Rcopper 1 0.440 C / W 1 98.34 C / W Rboard 0.438 C / W Maximum temperature occurs in the middle of the plate along the 20 cm length which is determined to be Tmax Tend Tboard ,total Tend Qi Rboard ,1 cm Tend Rboard ,1 cm Qi 30 C + (0.438 C / W)(15 +13.5 +12 +10.5 + 9 + 7.5 + 6 + 4.5 + 3 +1.5)W = 66.1 C 15 W 13.5 W 12 W 10.5 W 9W 7.5 W 6W 4.5 W 3W 1.5 W 30 C 1 cm Tmax Rboard 15-25 Chapter 15 Cooling of Electronic Equipment 15-65 A circuit board with uniform heat generation is to be conduction cooled by aluminum wires inserted into it. The magnitude and location of the maximum temperature in the PCB is to be determined. Assumptions 1 Steady operating conditions exist 2 Thermal properties are constant. 3 There is no direct heat dissipation from the surface of the PCB. Analysis The number of wires in the board is n 150 mm 4 mm 37 Double sided PCB 12 cm 15 cm Aluminum wire, D = 1 mm The surface areas of the aluminum wires and the remaining part of the epoxy layer are Aalu min um Atotal Aepoxy D2 (0.001 m) 2 n (37) 0.000029 m2 4 4 (length)( width) (0.003 m)(0.15 m) = 0.00045 m2 Atotal Aalu min um 0.00045 0.000029 0.000421 m2 4 mm Considering only half of the circuit board because of symmetry, the thermal resistance of each material per 1-cm length is determined to be Ralu min um Repoxy L kA L kA 0.01 m (237 W / m. C)(0.000029 m2 ) 0.01 m (0.26 W / m. C)(0.000421 m2 ) 1455 C / W . 9136 C / W . 3 mm Since these two resistances are in parallel, the equivalent thermal resistance is determined from 1 Rboard 1 Repoxy 1 Ralu min um 1 1455 C / W . 1 9136 C / W . Rboard 1432 C / W . Maximum temperature occurs in the middle of the plate along the 20 cm length which is determined to be Tmax Tend Tboard ,total Tend Qi Rboard ,1 cm Tend Rboard ,1 cm Qi 30 C + (1.432 C / W)(15 +13.5 +12 +10.5 + 9 + 7.5 + 6 + 4.5 + 3 +1.5)W = 148.1 C 15 W 13.5 W 12 W 10.5 W 9W 7.5 W 6W 4.5 W 3W 1.5 W 30 C 1 cm Tmax Rboard 15-26 Chapter 15 Cooling of Electronic Equipment 15-66 A thermal conduction module with 80 chips is cooled by water. The junction temperature of the chip is to be determined. Assumptions 1 Steady operating conditions exist 2 Heat transfer through various components is one-dimensional. Analysis The total thermal resistance between the junction and cooling water is Rtotal R junction water Junction Rchip 4W Rchip Rint ernal Rexternal 12 9 7 17.2 C . Rinternal Then the junction temperature becomes T junction Twater QR junction water 18 C + (4 W)(17.2 C/W) = 86.8 C Rexternal Cooling water 15-67 A layer of copper is attached to the back surface of an epoxy board. The effective thermal conductivity of the board and the fraction of heat conducted through copper are to be determined. Assumptions 1 Steady operating conditions exist 2 Heat transfer is one-dimensional. Analysis Heat conduction along a layer is proportional to the thermal conductivity-thickness product (kt) which is determined for each layer and the entire PCB to be (kt) copper (kt) epoxy (kt) PCB (386 W/m. C)(0.0001 m) (0.26 W/m. C)(0.0003 m) (kt) copper (kt) epoxy 0.0386 W/ C 0.000078 W/ C 0.038678 W/ C Copper, t = 0.1 mm PCB 15 cm 20 cm Q 0.0386 0.000078 Epoxy, t = 0.3 mm The effective thermal conductivity can be determined from k eff (kt) epoxy t epoxy (kt) copper t copper (0.0386 0.000078) W/ C (0.0003 m + 0.0001 m) 96.7 W/m. C Then the fraction of the heat conducted along the copper becomes f (kt) copper (kt) PCB 0.0386 W/ C 0.038678 W/ C 0.998 99.8% Discussion Note that heat is transferred almost entirely through the copper layer. 15-27 Chapter 15 Cooling of Electronic Equipment 15-68 A copper plate is sandwiched between two epoxy boards. The effective thermal conductivity of the board and the fraction of heat conducted through copper are to be determined. Assumptions 1 Steady operating conditions exist 2 Heat transfer is one-dimensional. Analysis Heat conduction along a layer is proportional to the thermal conductivity-thickness product (kt) which is determined for each layer and the entire PCB to be ( kt ) copper ( kt ) epoxy ( kt ) PCB (386 W / m. C)(0.0005 m) (2)(0.26 W / m. C)(0.003 m) ( kt ) copper ( kt ) epoxy 0193 W/ C . 0.00156 W/ C 019456 W/ C . Copper, t = 0.5 mm 12 cm 0193 0.00156 . Q The effective thermal conductivity can be determined from k eff (kt) epoxy t epoxy (kt) copper t copper (0.00156 0.193) W/ C (2 0.003 m) + 0.0005 m 29.9 W/m. C Then the fraction of the heat conducted along the copper becomes f (kt) copper (kt) PCB 0.193 W/ C 0.19456 W/ C 0.992 99.2% Epoxy, t = 3 mm 15-69E A copper heat frame is used to conduct heat generated in a PCB. The temperature difference between the mid section and either end of the heat frame is to be determined. Assumptions 1 Steady operating conditions exist 2 Heat transfer is one-dimensional. Analysis We assume heat is generated uniformly on the 6 in 8 in board, and all the heat generated is conducted by the heat frame along the 8-in side. Noting that the rate of heat transfer along the heat frame is variable, we consider 1 in 8 in strips of the board. The rate of heat generation in each strip is (20 W)/8 = 2.5 W, and the thermal resistance along each strip of the heat frame is R frame L kA (1/12) ft (223 Btu/h.ft. F)(6/12 ft)(0.06/12 ft) 0.149 h. F/Btu Tend 1 in 10 W PCB 6 in 8 in 8 in Heat frame Cold plate 7.5 W 5W 2.5 W Tmid Rboard Maximum temperature occurs in the middle of the plate along the 20 cm length. Then the temperature difference between the mid section and either end of the heat frame becomes Tmax Tmid section - edge of frame Qi R frame,1 in R frame,1 in Qi (0.149 F.h/Btu)(10 + 7.5 + 5 + 2.5 W)(3.4121 Btu/h.W) = 12.8 F 15-28 Chapter 15 Cooling of Electronic Equipment 15-70 A power transistor is cooled by mounting it on an aluminum bracket that is attached to a liquidcooled plate. The temperature of the transistor case is to be determined. Assumptions 1 Steady operating conditions exist 2 Conduction heat transfer is one-dimensional. Analysis The rate of heat transfer by conduction is Liquid channels Transistor 2 cm 2 cm Qconduction (080)(12 W) = 9.6 W . The thermal resistance of aluminum bracket and epoxy adhesive are Ralu min um Repoxy L kA L kA 0.01 m 0.703 C / W (237 W / m. C)(0.003 m)(0.02 m) 0.0002 m 1852 C / W . (1.8 W / m. C)(0.003 m)(0.02 m) Aluminum bracket The total thermal resistance between the transistor and the cold plate is Rtotal Rcase cold plate R plastic Repoxy Ralu min um 2.5 1852 0.703 5.055 C / W . Then the temperature of the transistor case is determined from Tcase Tcold plate QRcase cold plate 50 C + (9.6 W)(5.055 C/W) = 98.5 C 15-29
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Chapter 7 External Forced ConvectionChapter 7 EXTERNAL FORCED CONVECTIONDrag Force and Heat Transfer in External Flow 7-1C The velocity of the fluid relative to the immersed solid body sufficiently far away from a body is called the free-stream velocity
ASU - AET - AET432
Chapter 7 External Forced ConvectionFlow Across Cylinders And Spheres 7-35C For the laminar flow, the heat transfer coefficient will be the highest at the stagnation point which corresponds to 0 . In turbulent flow, on the other hand, it will be highest
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Chapter 7 External Forced Convection 7-52 A steam pipe is exposed to a light winds in the atmosphere. The amount of heat loss from the steam during a certain period and the money the facility will save a year as a result of insulating the steam pipe are t
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Chapter 7 External Forced Convection Special Topic: Thermal Insulation 7-73C Thermal insulation is a material that is used primarily to provide resistance to heat flow. It differs from other kinds of insulators in that the purpose of an electrical insulat
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Chapter 7 External Forced Convection 7-99 Wind is blowing over the roof of a house. The rate of heat transfer through the roof and the cost of this heat loss for 14-h period are to be determined. Assumptions 1 Steady operating conditions exist. 2 The crit
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Chapter 8 Internal Forced ConvectionChapter 8 INTERNAL FORCED CONVECTIONGeneral Flow Analysis 8-1C Liquids are usually transported in circular pipes because pipes with a circular cross-section can withstand large pressure differences between the inside
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Chapter 8 Internal Forced Convection 8-53 Hot air enters a sheet metal duct located in a basement. The exit temperature of hot air and the rate of heat loss are to be determined. Assumptions 1 Steady flow conditions exist. 2 The inner surfaces of the duct
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Chapter 8 Internal Forced ConvectionReview Problems 8-61 Geothermal water is supplied to a city through stainless steel pipes at a specified rate. The electric power consumption and its daily cost are to be determined, and it is to be assessed if the fri
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Chapter 9 Natural ConvectionChapter 9 NATURAL CONVECTIONPhysical Mechanisms of Natural Convection 9-1C Natural convection is the mode of heat transfer that occurs between a solid and a fluid which moves under the influence of natural means. Natural conv
ASU - AET - AET432
Chapter 9 Natural Convection 9-32 A fluid flows through a pipe in calm ambient air. The pipe is heated electrically. The thickness of the insulation needed to reduce the losses by 85% and the money saved during 10-h are to be determined. Assumptions 1 Ste
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Chapter 9 Natural ConvectionCombined Natural and Forced Convection 9-72C In combined natural and forced convection, the natural convection is negligible when Gr / Re2 01 . Otherwise it is not. . 9-73C In assisting or transverse flows, natural convection
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Chapter 9 Natural ConvectionReview Problems 9-94E A small cylindrical resistor mounted on the lower part of a vertical circuit board. The approximate surface temperature of the resistor is to be determined. Assumptions 1 Steady operating conditions exist
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Chapter 9 Natural Convection 9-103E The components of an electronic device located in a horizontal duct of rectangular cross section is cooled by forced air. The heat transfer from the outer surfaces of the duct by natural convection and the average tempe
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Chapter 10 Boiling and CondensationChapter 10 BOILING AND CONDENSATIONBoiling Heat Transfer10-1C Boiling is the liquid-to-vapor phase change process that occurs at a solid-liquid interface when the surface is heated above the saturation temperature of
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Chapter 10 Boiling and Condensation 10-21 Water is boiled at 1 atm pressure and thus at a saturation (or boiling) temperature of Tsat = 100 C by a horizontal nickel plated copper heating element. The maximum (critical) heat flux and the temperature jump o
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Chapter 10 Boiling and CondensationCondensation Heat Transfer10-34C Condensation is a vapor-to-liquid phase change process. It occurs when the temperature of a vapor is reduced below its saturation temperature Tsat. This is usually done by bringing the
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Chapter 10 Boiling and Condensation Review Problems 10-72 Steam at a saturation temperature of Tsat = 40 C condenses on the outside of a thin horizontal tube. Heat is transferred to the cooling water that enters the tube at 25 C and exits at 35 C. The rat
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Chapter 11 Fundamentals of Thermal RadiationChapter 11 FUNDAMENTALS OF THERMAL RADIATIONElectromagnetic and Thermal Radiation11-1C Electromagnetic waves are caused by accelerated charges or changing electric currents giving rise to electric and magneti
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Chapter 11 Fundamentals of Thermal RadiationAtmospheric and Solar Radiation11-50C The solar constant represents the rate at which solar energy is incident on a surface normal to sun's rays at the outer edge of the atmosphere when the earth is at its mea
UCLA - ACCOUNTING - 120b
CHAPTER 9Inventories: Additional Valuation IssuesASSIGNMENT CLASSIFICATION TABLE (BY TOPIC)Topics 1. Lower-of-cost-or-market. 2. Inventory accounting changes; relative sales value method; net realizable value. 3. Purchase commitments. 4. Gross profit m
SUNY Oneonta - MGMT - 241
Typical Managerial Functions at a CompanyStaffing, hiring, terminating. Wage levels and payroll. Employee development and motivating Division of work and departmentalizin Organizing, creating hierarchies and chain of command Dept A Dept C Dept D Dept BL
Kaplan University - BU204 - 204-08
1. What of the following will NOT cause an increase on demand for good X? a decrease in the price of good X 2. A good is inferior if_. When income increases, demand decreases 3. A technological advance in the production of automobiles will_. Increase the
USC - BISC - 150
Commentary on Lecture 7Feb. 3, 2009Osteoporosis is a name that literally means " bones with holes" which, of course, weakens them. There are two forms of this partially nutritional, partially environmental disease. The one that affects very young childr
USC - BISC - 150
Commentary on Lecture 6 Jan. 29, 2009 During Tuesday's lecture I neglected to talk about a promising treatment for Type 1 diabetes. It's called the Edmonton Protocol because it's a procedure (protocol) devised by researchers in Edmonton, Alberta, Canada.
USC - BISC - 150
Commentary on Lecture 5Jan. 27, 2009Contrary to the current fad diets, your body thinks carbohydrates (glucose) as an important component of your daily diet. Why else would it make such an effort to maintain a relatively constant blood glucose level? Gl
USC - BISC - 150
Commentary on Lecture 4 Jan. 22, 2009 On Tuesday we went over the rules governing the interactions of atoms with each other. The kind of chemical reaction that will occur depends upon the number of electrons that are in the valence shell of each of the at
USC - BISC - 150
Commentary on Lecture 3 Sept. 2, 2008 Today's lecture was about the rules governing chemical reactions between atoms. Atoms of all the different chemical elements are built using the same pattern: a central core called the nucleus in which a number of pro
USC - BISC - 150
Commentary on Lecture 2 Aug.28, 2008 The components of the macronutrients are interrelated. While glucose is the preferred energy source it is also used as the basis for synthesizing the 10 kinds of amino acids we are capable of making. The other 10 as we