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4. Air concentrated with solute P is brought in contact with water. At steady state, the bulk concentration of P in air and water are 0.3 and 0.02 respectively. The equilibrium equation relating the interface composition is $y_{p,i} = 0.25x_{p,i}$. Assume that the mass transfer co-efficient $F_G = F_L$ are identical. The gas phase mole fraction of P at the interface ($y_{p,i}$) is

          4. Air concentrated with solute P is brought in contact with water. At steady state, the bulk
concentration of P in air and water are 0.3 and 0.02 respectively. The equilibrium
equation relating the interface composition is $y_{p,i} = 0.25x_{p,i}$. Assume that the mass
transfer co-efficient $F_G = F_L$ are identical. The gas phase mole fraction of P at the
interface ($y_{p,i}$) is

$4. Air concentrated with solute P is brought in contact with water. At steady state, the bulk concentration of P in air and water are 0.3 and 0.02 respectively. The equilibrium equation relating the interface composition is yp,i = 0.25xp,i. Assume that the mass transfer co-efficient FG = FL are identical. The gas phase mole fraction of P at the interface (yp,i) is$

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