If we assume the vapor pressures are the ratios of the temperature ratios (150/130) and then plug it into the Fenske equation.
N = log [(Xd /(1 - Xd) x (1 -
Xb) / Xb} / log avg
where:
N = minimum number of theoretical plates required at total reflux
(of which the reboiler is one)
Xd = mole fraction of more volatile component in the
overhead distillate 0.99
Xb = mole fraction of more volatile component in the
bottoms assume 0.50
avg =
average relative volatility of more volatile component to less
volatile component (150/130)
N = log { 0.99 / (1 - 0.99) x (1 -.0.50) / 0.50) } / log (1.15)
N = log { 0.99 / (0.01) x (0.50) / 0.50) } / log (1.15)
N = log (99 x 1) / log 1.15
N = 1.99/0.061
N = 32.6 theoretical plates.
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