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Heat Transfer

Heat Transfer
For an ideal black body

Transmissivity = 1
Absorptivity = 1
Emissivity = 0
Reflectivity = 1

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Heat Transfer
In forced convection, the heat transfer depends on

Re, Gr
none of the listed here
mainly Gr
Re, Pr

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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
12.0 kW/m²
16.5 kW/m²

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Heat Transfer
Film boiling is usually not desired in commercial equipments, because

it is difficult to maintain
the heat transfer rate is low in view of the large temperature drop. @
it is not economic
none of the listed here

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Heat Transfer
Grashhoff number is given by

gD³βΔtP²/μ
gD³.β.Δtρ²/μ²
gD2βΔtP²μ
gD2βΔtρ/μ²

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Heat Transfer
Bulk of the convective heat transfer resistance from a hot tube surface to the fluid flowing in it, is

In the central core of the fluid
None of these
Uniformly distributed throughout the fluid
Mainly confined to a thin film of fluid near the surface

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MORE MCQ ON Heat Transfer

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