12.
For a liquid in laminar flow through a very long tube, when the exit fluid temperature approaches the wall temperature, the equation to be used is

13.
In case of a vertical tube evaporator, with increase in the liquor level, the

16.
A sphere of radius 'R1' is enclosed in a sphere of radius 'R2'. The view (or shape) factor for radiative heat transfer of the outer sphere with respect to the inner sphere is

20.
Tubes are held between top and bottom tube sheets in Calenderia type evaporator by keeping

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