Mass Transfer
In case of absorption, both the operating and equilibrium lines will be straight for

Dilute solutions
Isothermal operation
Dilute solutions and isothermal operation
None of these

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Mass Transfer
Fenske's equation for determining the minimum number of theoretical stages in distillation column holds good, when the

Multicomponent distillation is involved
Mixture (to be separated) shows positive deviation from ideality
Mixture (to be separated) shows negative deviation from ideality
Relative volatility is reasonably constant

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