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A process fluid having a specific heat of
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- 5. Hot exhaust gases, which enter a finned-tube, cross-flow heat exchanger at 300 °C and leave at 100 °C, are used to heat pressurized water at a flow rate of 1 kg/s from 35 °C 125 °C. The specific heat of water at the average water temperature is 4197 J/kg. K. The overall heat transfer coefficient based on the gas-side surface area is Uh = 100 W/m².K. Determine the required gas-side surface area A₁ using the LMTD and & -NTU method.arrow_forwardPlease explain with steps.arrow_forwardHot water at 60℃ is cooled to 36℃ through the tube side of a 1–shell pass and 2-tube passesheat exchanger. The coolant is also a water stream, for which the inlet and outlet temperaturesare 7℃ and 31℃, respectively. The overall heat transfer coefficient and the heat transfer areaare 950 W/m2 K and 15 m2 , respectively. Calculate the mass flow rates of hot and cold waterstreams in steady operation. (Answers: 3.63 kg/s for both stream)arrow_forward
- Please only first attempt (or you will be downnvoted)arrow_forwardIn a double-pipe, counter-flow heat exchanger, water entering at 1 kg/s is heated from 23°C to 69°C as it flows thru the inner pipe. Hot oil enters the heat exchanger at 2 kg/s and 110°C. The convection heat transfer coefficients in the cold- and hot-sides are 100 and 50 kW/m2.0C, respectively. Calculate the required heat transfer area in m?. Take cp = 4.18 kJ/kg.°C for water, and cCp = 1.67 kJ/kg.°C for oil. Round your answer to 2 decimal places. Add your answerarrow_forwardA counterflow, concentric tube heat exchanger used for engine cooling has been in service for an extended period of time. The heat transfer surface area of the exchanger is 5 m^2, and the design value of the overall convection coefficient is 38 W/m^2-K. During a test run, engine oil flowing at 0.1 kg/s is cooled from 110°C to 66°C by water supplied at a temperature of 25°C and a flow rate of 0.2 kg/s. Determine whether fouling has occurred during the service period. If so, calculate the fouling factor, R"f(m^2• K/W).arrow_forward
- A long, thin-walled double-pipe heat exchanger with tube and shell diameters of 0.01 m and 0.025 m, respectively, is used to condense refrigerant-134a with water at 20°C. The refrigerant flows through the tube, with a convection heat transfer coefficient of hi= 4100 W/m² °C. Water flows through the shell at a rate of 0.3 kg/s. The thermal resistance of the inner tube is negligible since the tube material is highly conductive and its thickness is negligible. Both the water and refrigerant-134a flows are fully developed. Properties of the water and refrigerant-134a are constant. Water properties: p = 998 kg/m³, v=u/p-1.004x 10-6 m²/s, k = 0.598 W/m. °C, Pr = 7.01 Cold water D Doarrow_forwardA hot oil is to be cooled by cold water in one shell-pass 8 tube passes heat exchanger. If the surface area of the pipes is 3 m? and the overall heat transfer coefficient U is 315 W/m.K. The cold water enters the tubes at 20C with a mass flow rate of 0.4 kg /s and the oil enters the shell at 150°C with a mass flow rate of 0.6 kg /s. Take c, for water as 4.20 kJ/kg.°C and for oil as 2.10 kJ/kg.K. Calculate a) The heat transfer rate for this heat exchanger b) The outlet temperature of water .c) The outlet temperature of oil Oil Waterarrow_forwardA body is desired to be heated with hot water and oil on the body side in a heat exchanger with 20 pipe passes. The inner and outer diameters of the copper pipe are 20 and 24 mm, respectively. Water with a flow rate of 0.2 kg / s enters the pipe at 87 ° C and leaves at 43 ° C. The inlet and outlet temperatures of the oil in the heat exchanger are 7 ° C and 37 ° C, respectively. Average heat transfer coefficient on the outer surface of the pipes is 800 W / m ° K. The fouling resistances on both sides are negligible.Determine;a) Heat transfer b) External surface based total heat transfer coefficient, c) Determine the pipe length in one pass.arrow_forward
- Read the question carefully and give me right solution with clear calculations. Thank youarrow_forwardA one-shell pass and two-tube passes heat exchanger cools 1.8 L/s of oil (cp = 2.5 kJ/kg-K and density = 720 kg/m3) from 94 C to 48 C. Cooling water enters the tubes at 15 C and leaves at 40 C. The overall coefficient of heat transfer is 450 W/m2-K. Fouling of the tubes occurs, resulting in one-quarter of the tubes being blocked. The conditions remain the same except for the outlet temperatures. Determine the (a) oil exit temperature (1 decimal place) and (b) water exit temperature (1 decimal place) under the new condition.arrow_forwardGlycerin (cp=2400 J/kg*K) at 20°C and 1 kg/s is to be heated by ethylene glycol (cp = 2500 J/kg*K) at 75°C and the same mass flow rate in a thin-walled double-pipe parallel-flow heat exchanger. If the overall heat transfer coefficient is 380 W/m²*K and the pipe is 75m long and 2.5cm in diameter, determine (a) the rate of heat transfer and (b) the outlet temperatures of the glycerin and the glycol.arrow_forward
- Principles of Heat Transfer (Activate Learning wi...Mechanical EngineeringISBN:9781305387102Author:Kreith, Frank; Manglik, Raj M.Publisher:Cengage Learning