Heat Transfer
The average heat transfer co-efficient for laminar film condensation on vertical surface is inversely proportional to (where, ΔT = Temperature drop across condensate film )

(ΔT)1/4
(ΔT)2
None of the listed here
ΔT

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Heat Transfer
Fouling factor

Is a dimensionless quantity
Does not provide a safety factor for design
None of these
Accounts for additional resistances to heat flow

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Heat Transfer
A process stream of dilute aqueous solution flowing at the rate of10 Kg.s⁻¹ is to be heated. Steam condensate at 95°C is available for heating purpose, also at a rate of 10 Kg.s⁻¹. A 1 - 1 shell and tube heat exchanger is available. The best arrangement is

Counter flow with process stream on shell side
Parallel flow with process stream on tube side
Counter flow with process stream on tube side
Parallel flow with process stream on shell side

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