Heat Transfer
Log mean temperature difference (LMTD) cannot be used, if

there exists an unsteady state
the heat capacity is not constant and there is a phase change.
none of the listed here
heat transfer co-efficient over the entire heat exchanger is not constant

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

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