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A steel tube
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- A double tube heat exchanger is made of copper (k=380 W/m.°C). Inner diameter of inner tube Di=1.2 cm, outer diameter D0=1.6 cm and the diameter of the outer tube is 3.0 cm. Convection heat transfer coefficient on the inner surface of the pipe hi=700 W/m2 .°C and the heat transfer coefficient on the outer surface h0= 1400 W/m2 .°C. on the pipe side contamination factor Rf,i=0.0005 m2 .°C/W and the contamination factor on the body side Rf,0 = 0.0002 m2 .°C/W as it is; a) The thermal resistance of the heat exchanger per unit length, b) Total heat transfer coefficients (U0 and Ui) taking into account the inner and outer surface areas of the pipe calculate.arrow_forwardA double tube heat exchanger is made of copper (k = 380 W / m. ° C). Inner diameter of inner tube Di = 1.2 cm, outerits diameter is D0 = 1.6 cm and the diameter of the outer pipe is 3.0 cm. Convection heat transfer coefficient on the inner surface of the pipehigh = 700 W / m2. ° C and the heat transfer coefficient on the outer surface h0 = 1400 W / m2. ° C. Pipe sidecontamination factor Rf, i = 0.0005 m2. ° C / W and fouling factor Rf on the body side, 0 = 0.0002 m2. ° C / WAccording to the example; Calculate the thermal resistance of the heat exchanger per unit length.arrow_forwardQuestion 6: Find the required length of a 5 cm-diameter tube to heat water from an inlet temperature of 30 °C to an outlet temperature of 100 °C using either: a) Constant temperature of 200 °C, or b) Constant heat flux of 10,000 W/m?. The mass flow rate of the water is 0.5 kg/s, its thermal conductivity is 0.04 W/m.K and its specific heat is 4190 kJ/kg.K. Assume a fully-developed flow.arrow_forward
- The hot gas temperature in a heat exchanger is 350 deg C (ho=220 W/m2-K). What is the surface temperature on the wall if the heat transferred is 1500 W/m2? Select the correct response: 358 deg C 350 deg C 338 deg C 343 deg Carrow_forward(2.23) A finned heat exchanger tube is made of aluminum alloy (k = 186 W/m · K) and contains 125 annular fins per meter of tube length. The bare tube between fins has an OD of 50 mm. The fins are 4 mm thick and extend 15 mm beyond the external surface of the tube. The outer surface of the tube will be at 200°C and the tube will be exposed to a fluid at 20°C with a heat-transfer coefficient of 40 W/m2 · K. Calculate: (a) The rate of heat transfer per meter of tube length for a plain (un-finned) tube. (b) The fin efficiency. (c) The fin and prime surface areas per meter of tube length. (d) The weighted efficiency of the finned surface. (e) The rate of heat transfer per meter of tube length for a finned tube. (f) If the cost per unit length of finned tubing is 25% greater than for plain tubing, determine whether plain or finned tubing is more economical for this service. %3D Ans. (a) 1130 W. (b) 98.6%. (c) 0.8946 m? and 0.07854 m². (d) 98.7%. (e) 6920 W.arrow_forwardElectric heater wires are installed in a solid wall having a thickness of 8 cm and k=2.5W/m- °C. The right face is exposed to an environment with h=50W/m^ 2 . C and T infty =30^ C , while the left face is exposed to h=75 W/m^ 2 C T infty =50^ C . What is the maximum allowable heat-generation rate such that the maximum tem perature in the solid does not exceed 300 degrees * C ?arrow_forward
- copper determine the overall heat transfer coefficient of a condenser formed of pipe when the fluid-side heat-transfer coefficient is 2000 W/m². °C and the heat-transfer coefficient on the refrigerant side is 1200 W/m². °C. The pipe has an outside diameter of 25.4 mm and an inside diameter of 19.8 mm. The thermal conductivity of steel is (410) W/m °C.arrow_forwardA cylindrical reactor made of copper with a radius of a= r=5mm has a heat conduction coefficient of k=386 W/moC, and there is heat generation at e ̇= (q ) ̇= 4x10^8 W/m3 inside this reactor. The cylindrical reactor convection heat transfer coefficient is h=2000 W/m0C and 〖T_(ambient= ) T〗_∞= 30 oC by convection, it cools down from the reactor surface to the center. According to the given boundary conditions a)Find the reactor surface temperature and the temperature T(a) at r=a. (VARIABLES: r=1-10mm, T_∞= 0-100oC) b) q(a) =((q ) ̇ * a )/ 2 = (e ̇ * a )/ 2 then find the heat flux amount in kW/m2arrow_forwardQ1] A shell and tube heat exchanger is used to heat water (C = 4236 J/kg. °C) from 80°C to 150°C at a rate of 12.5 kg/s by hot gas that enters the exchanger at 350°C with a rate of 20.36 kg/s. The overall heat transfer coefficient is 290 W/m² °C. The gas making 2-shell passes and the water making 4-tube passes. Calculate the heat transfer surface area (Cp (gas) = 1.04 kJ/kg.°C). heat flux: (a) byarrow_forward
- Blowtorch is used to connect the two pipes together. Length of the pipe section shown is 150 cm with an inner diameter of 85 cm. The thickness of the pipe wall is 4 mm. The conductivity of the pipe section is 167 Wim^2K. Environment has a temperature of 30 C and convective heat transfer coefficient of 28 WI(mC), find the required heat transfer to join the pipe sections at 220 C? HINT: Assume that the welding section is the base plate and the pipe is 1D extended surface (fin) symmetric about the torch melting line. Heat transfer happens by conduction along the pipe thíckness in horizontal direction and by convection to the environment. Length thickness Torch melting line 200 W 275 W none 314 W 453 Warrow_forwardQ1: A shell-and-tube heat exchanger having one shell pass and four tube passes is shown schematically in the following sketch. The fluid in the tubes enters at 200°C and leaves at 100°C. The temperature of the fluid is 20°C entering the shell and 90°C leaving the shell. The overall heat transfer coefficient based on the surface area of 12 m² is 300 W/m² K. Calculate the heat transfer rate between the fluids. +4 Tube fluid 200 °C Tube fluid 100 °C Shell fluid 90 °℃ M 41: Shell fluid 20°Carrow_forwardA double-pipe heat exchanger is constructed of a copper (k = 380 W/m⋅K) inner tube of internal diameter Di = 1.2 cm and external diameter Do = 1.6 cm and an outer tube of diameter 3.0 cm. The convection heat transfer coefficient is reported to be hi = 700 W/m2⋅°C on the inner surface of the tube and ho = 240 W/m2⋅°C on its outer surface. The fouling factor is Rf, i = 0.0005 m2⋅°C/W on the tube side and Rf, o = 0.0002 m2⋅°C/W on the shell side. Determine the thermal resistance of the heat exchanger per unit length. The thermal resistance of the heat exchanger per unit length is _____ °C/W.arrow_forward
- Principles of Heat Transfer (Activate Learning wi...Mechanical EngineeringISBN:9781305387102Author:Kreith, Frank; Manglik, Raj M.Publisher:Cengage Learning