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Fundamentals of Heat and Mass Transfer
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- 5.0 Air at p=p= 1 atm enters a thin-walled (D=D= 5-mm diameter) long tube (L=L= 2 m) at an inlet temperature of Tm,i=Tm,i= 100°C. A constant heat flux is applied to the air from the tube surface. The air mass flow rate is m˙ =m˙ = 125 × 10-6 kg/s. If the tube surface temperature at the exit is Ts,o=Ts,o= 160°C, determine the heat rate entering the tube, in W. Evaluate properties at T=T=400 K.arrow_forwardConcentric tube heat exchanger (tubular or tube in tube) is used for a large industrial gas turbine. The dimensions and values are given. One of the steps is not required to find the required length of the HX, if the oil leaves at 60 C? Oil and water inlet temperatures are 100 and 30 C, respectively. Thermal entry length to validate the steps O None of the above Log mean temperature difference Reynolds number, Prandtl number and Nusselt number O Overall heat transfer coefficientarrow_forwardSteam condensing at 120°C (h, = 2203 kJ/kg) on the shell side of (1 shell and 12 thin-walled tubes) heat exchanger. Water (18 °C, C, =4180 J/kg-"C) enters the tube @ 3.4 kg/s ấnd the temperature difference between the two fluids at the exit is 57°C, assume LMTD correction factor of 1.0, for each tube: length = 2.7 m, diameter = 2.4 cm. What is the overall heat transfer coefficient (W/m¯.°C)? Select bne: O A. 2234.41 O B. 3859.43 C. 3385.47 D. 2979.21 E. 2606.81arrow_forward
- A heat exchanger with an effectiveness of 75 percent is used to heat 5 kg/s of water from 2. ( 50 °C with condensing steam at 1 atm. Calculate the area for U = 1200 W/m2.°C. Suppose fouling occurred on both the tube and shell side with the following fouling factors, Rwater = 0.0002 m2-°C/W, and Risteam = 0.00009 m2. °C/W, what will be the new exiting temperature of the water?arrow_forwardSteam condensing at 120°C (h =2203 kJ/kg) on the shell side of (1 shell and 12 thin- walled tubes) heat exchanger. Water (18 °C, C_ =4180 J/kg-°C) enters the tube @ 3.3 kg/s and the temperature difference between fhe two Uuits at the exit is 55°C, assume LMTD correction factor of 1.0, for each tube: length =2.7 m, diamieter = 2.4 cm. What is the rate of condeusation of steam (kg/inin) Select one OA 17.66 OB.21.37 OC. 13.77 OD. 15.72 OE 1960arrow_forwardFigure shows a heat exchanger designed to cool 5250 kg/h of an ethyl alcohol solution (Cp = 3810 J/kg. °C) from 66 °C to 39 °C.Water (Cp = 4200 J/kg. °C) at 10 °C is pumped at 4750 kg/h to cool the solution. The tube side fluid flows in a circular pipe with an outside diameter of 25 mm. The overall heat transfer coefficient is (6.84x10^2) W/(m².°C). Find the tube length 'L' for one pass of a two-pass parallel flow double-pipe heat exchanger as shown in Figure. Answer should be in m with three significant figures.arrow_forward
- In a large student house supply at a pressure of 2 bar, gauge, and at a temperature 10°C. A wash basin cold tap is located 3 meters above the mains supply, connected to the mains pipe with a copper pipe of internal diameter 15 mm and length 12 meters. When the tap is opened the flow rate of water out of the tap is 24 litres per minute, creating a Fanning friction factor in the pipe of 0.008. cold water is supplied by the mains water a) Calculate the Reynolds number of the water in the pipe and determine if it is laminar or turbulent. b) Calculate the pressure loss from friction, change in elevation, and hence the pressure of the water just before entering the tap. c) Name two assumptions that have been made in order to arrive at your answer to part b) and state if these assumptions under or over predict the pressure of the water just before entering the tap. d) If the value were not given, what procedure would be needed to determine the Fanning friction factor?arrow_forward8.51 Consider a thin-walled, metallic tube of length L 1 m and inside diameter D 3 mm. Water enters the tube at m 0.015 kg /sm-0.015 kg/s and Tm.i=97°C. a. What is the outlet temperature of the water if the tube surface temperature is maintained at 27 C? ( b. If a 0.5-mm-thick layer of insulation of k = 0.05 W/m-K is applied to the tube and its outer surface is maintained at 27°C, what is the outlet temperature of the water? c. If the outer surface of the insulation is no longer maintained at 27°C but is allowed to exchange heat by free convection with ambient air at 27°C, what is the outlet temperature of the water? The free convection heat transfer coefficient is 5 W/m-Karrow_forwardSteam condensing at 120°C (h = 2203 kJ/kg) on the shell side of (1 shell and 12 thin-walled tubes) heat exchanger. Water (18 °C, C, =4180 J/kg-°C) enters the tube @ 2.9 kg/s and the temperature difference between the two fluids at the exit is 42°C, assume LMTD correction factor of 1.0, for each tube: length = 2.7 m, diameter = 2.4 cm. What is the overall heat transfer coefficient (W/m .°C)? "fg Select one: A. 4402.97 B. 2905.96 C. 5019.38 D. 3390.28 E. 3874.61arrow_forward
- PROBLEM Ħ 22.a. mass at a pressure the temperature of hot water is being 248.09 °F to 212.09 °F using a heat exchanger. = 2at m and flow rate = 1020 kg /min, decreased from oF using Reservvir waten s used as coolant with mass flow rate = 1800 kalmin and kg Imin inlet temperature = 50.09 oF. 2 The minimun allow able ft? surface are a= 270. 17 of heat ex changer all ow able overall heat = 206.05 btul The transfer coefficient of heat exchanger maximem do z7f4 The heat capací ty to be used must he the average value of inlet and out let temperatures. Hind the Number of Transfer units (NTU) using effective nes NTU Method if the heat exch anger being used is heat exchang er (specify which fluid is mixed or unmixed Cross flowarrow_forwardA double tube heat exchanger will be used to cool bezene from 82 Celsius to 38 Celsius. water enters the annular space at 21 Celsius, flows countercurrent with benzene at 1.5 m / s, exiting at 37 Celsius. The internal tubing is 1 1/4 inch cd 40 of commercial steel. The outer tubing is 2-inch Cd 40 steel. What is the heat transfer coefficient that would be expected for water? the fluid moves in the annular space of the two tubes that are concentric. there is a formula for that. h = 6,206 kcal / hm ^ 2 ° Carrow_forwardSteam condensing at 120°C (h, kJ/kg) on the shell side of (1 snell and 12 thin-walled tubes) heat exchanger. Water (18 °C, C, =4180 J/kg-°C) enters the tube @ 2.9 kg/s and the temperature difference between the two fluids at the exit is 42°C, assume LMTD correction factor of 1.0, for each tube: length = 2.7 m, diameter = 2.4 cm. What is the rate of condensation 2203 "fg %3D of steam (kg/min) ? Select one: А. 17.63 В. 21.99 C. 23.97 D. 15.45 Е. 19.81arrow_forward
- Principles of Heat Transfer (Activate Learning wi...Mechanical EngineeringISBN:9781305387102Author:Kreith, Frank; Manglik, Raj M.Publisher:Cengage Learning