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

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

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

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

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