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Heat Transfer

Heat Transfer
Reynold's analogy states that

Nst α f
Nst α NRe
NRe α f
NNu α f

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Heat Transfer
Natural convection is characterised by

Peclet number
Prandtl number
Grashhoff number
Reynolds number

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Heat Transfer
Maximum water velocity in tubes of a 1-2 shell and tube heat exchanger may be around __________ metres/second.

10
30
1
20

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Heat Transfer
Multiple effect evaporation accounts for

Investment economy
Steam economy
Lower operating costs
None of these

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Heat Transfer
For __________ Prandtl number values, the heat conduction will be negligible in the buffer zone.

Low
High
No
Extremely low

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Heat Transfer
When vaporisation takes place through a blanketting film of gas, the phenomenon is termed as __________ boiling.

film
none of the listed here
pool
transition

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