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Heat Transfer

Heat Transfer
Agitated film evaporator is suitable for concentrating __________ liquids.

Very thin
Corrosive
Viscous
Foaming

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Heat Transfer
Reason for operating an evaporator in multiple effect is to secure

Increased capacity
Both A and B
Decreased steam consumption
Increased steam economy

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Heat Transfer
Steady state one dimensional heat flow by conduction as given by Fourier's low does not assume that

There is no internal heat generation
Material is anisotropic
Boundary surfaces are isothermal
Constant temperature gradient exists

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Heat Transfer
The radiation heat flux from a heating element at a temperature of 800°C, in a furnace maintained at 300°C is 8 kW/m². The flux, when the element temperature is increased to 1000°C for the same furnace temperature is

11.2 kW/m²
14.6 kW/m²
16.5 kW/m²
12.0 kW/m²

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Heat Transfer
A metal ball of radius 0.1 m at a uniform temperature of 90°C is left in air at 30°C. The density and the specific heat of the metal are 3000 kg/m³ and 0.4 kJ/kg.K respectively. The heat transfer co-efficient is 50 W/m².K Neglecting the temperature gradients inside the ball, the time taken (in hours) for the ball to cool to 60°C is

0.15
555
0.55
55.5

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Heat Transfer
Steam economy in case of a triple effect evaporator will be

1
< 1
> 1
Between 0 and 1

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