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Nicholas Mogoi verified

Numerade educator

In a heating system, cold outdoor air at 7 潞C flowing at a rate of 4 kg/min is mixed adiabatically with heated air at 70 潞C flowing at a rate of 3 kg/min. The exit mass flow of the mixture is

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Penny Riley verified

Numerade educator

A double-pipe heat exchanger is constructed of a copper (k = 380 W/m 路 掳C) inner tube of internal diameter Di = 2.2 cm and external diameter Do = 2.6 cm and an outer tube of diameter 5.0 cm. The convection heat transfer coefficient is reported to be hi = 800 W/m2 路 掳C on the inner surface of the tube and ho = 1400 W/m2 路 掳C on its outer surface. For a fouling factor Rf, i = 0.0006 m2 路 掳C/W on the tube side and Rf, o = 0.0008 m2 路 掳C/W on the shell side, determine overall heat transfer coefficient Uo based on outer diameter a)270 W b)319 kW/m^2.C c)270 kW/m^2.C d)319 W/m^2.C e)270 W/m^2.C

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Nicholas Mogoi verified

Numerade educator

Water at an average temperature of 107掳C and an average velocity of 3.5 m/s flows through a 5-m-long stainless steel tube (k = 14.2 W/m 路 掳C) in a boiler. The inner and outer diameters of the tube are Di =1.0 cm and Do = 1.4 cm, respectively. If the convection heat transfer coefficient at the outer surface of the tube where boiling is taking place is ho= 8400 W/m2 路 掳C, determine the overall heat transfer coefficient Ui of this boiler based on the inner surface area of the tube. Take 蠀=0,268 x 10-6 m2/s, k=0,682 W/m.K, Pr=1,58 for water at 107 潞C. Neglect fouling resistance at the inner and outer part of the tube. a) 3500 W/m^2.C b) 5887 kW/m^2.C c) 5887 W/m^2.C d) 3501 kW/m^2.C e) 5887 kW

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Penny Riley verified

Numerade educator

A 6 m wide 2.8 m high wall is constructed of one layer of common brick (k=0.72 W/m.鈦癈) of thickness 20 cm, one inside layer of light weight plaster (k=0.36 W/m.鈦癈) of thickness 1 cm, and one outside layer of cement based covering (k=1.40 W/m.鈦癈) of thickness 2 cm. The inner surface at 13 oC is exposed to outdoors at 8 鈦癈 with a combined convection and radiation heat transfer coefficient of 17 W/m2.鈦癈. Determine the rate of heat transfer through the wall

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Glycerin (Cp= 2400 J/kg 路 掳C) at 20掳C and 0.3 kg/s is to be heated by ethylene glycol (Cp=2500 J/kg 路 掳K) at 60 掳C in a thin-walled double-pipe parallel-flow heat exchanger. The temperature difference between the two fluids is 15掳C at the outlet of the heat exchanger. If the overall heat transfer coefficient is 240 W/m2 路 掳K and the heat transfer surface area is 3.2 m2, determine the outlet temperature of the glycerin a)57.2 C b)47.2 C c)47.2 K d)320.2 C e)47.2 R

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Nishant Kumar verified

Numerade educator

An apple with an average mass of 1.8 kg and average specific heat of 3.65 kJ/kg.潞C is cooled from 22 潞C to 5 潞C. The amount of heat transferred from the apple is a)112J b)11.2 kJ c)112 kJ d)62.1 kJ e)11.2 kJ

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