Fouling Factor R and Overall Heat Transfer Coefficient U
Автор: Brian Bernard
Загружено: 2025-02-16
Просмотров: 768
Описание:
Heat Transfer Example Problem involving the Fouling Factor R, Overall Heat Transfer Coefficient U, Convection Internal Flow calculated using the Dittus-Boelter Equation to find the Nusselt Number and heat transfer coefficient h, Reynold's Number to find internal turbulent flow, and thermal resistance due to conduction through a cylindrical surface. This fouling factor example problem is also an overall heat transfer coefficient example problem.
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• Heat Transfer
CHAPTERS
0:00 What is Heat Transfer Fouling Factor R?
2:02 Thermal Circuit Thermal Resistance
5:39 Dittus-Boelter Equation Turbulent Internal Flow
8:59 Find Overall Heat Transfer Coefficient U
Water at an average temperature of 110 C and an average velocity of 3.5 m/s flows through a 7-m-long stainless steel tube (k = 14.2 W/m k) in a boiler … determine the overall heat transfer coefficient U of this boiler based on the inner surface area of the tube. Assume a fouling factor Rfi = 0.0005 m2K/W on the inner surface of the tube.
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