Steam 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 @ 3.3kg/s and the temperature difference between fhe two Uuits at the exit is 55°C, assumeLMTD correction factor of 1.0, for each tube: length =2.7 m, diamieter = 2.4 cm. Whatis the rate of condeusation of steam (kg/inin)Select oneOA 17.66OB.21.37OC. 13.77OD. 15.72OE 1960

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Steam 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 ihe two fluids at he exit is 55C, assume LMTD correction factor of 1.0, for each tube: length =2.7 m, diameter =2.4 cm. What s the rate of condensation of steam (kg/inin)R Select one OA 17.66 OB.21.37 OC. 13.77 OD. 15.72 OE 1960

Steam 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 ihe two fluids at he exit is 55C, assume LMTD correction factor of 1.0, for each tube: length =2.7 m, diameter =2.4 cm. What s the rate of condensation of steam (kg/inin)R Select one OA 17.66 OB.21.37 OC. 13.77 OD. 15.72 OE 1960

Principles of Heat Transfer (Activate Learning with these NEW titles from Engineering!)

8th Edition

ISBN:9781305387102

Author:Kreith, Frank; Manglik, Raj M.

Publisher:Kreith, Frank; Manglik, Raj M.

Chapter6: Forced Convection Over Exterior Surfaces

Section: Chapter Questions

Problem 6.53P

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