assuming the validity of r a nulls law do the following calculations for the benzene1 toluene2 s

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Assuming the validity of Raoult's law, do the following calculations for the benzene(1) / toluene(2) system: (a) Given x1 = 0.33 and T = 100°C, find y1 and P. (b) Given y1 = 0.33 and T = 100°C, find x1 and P. (c) Given x1 = 0.33 and P = 120 kPa, find y1 and T. (d) Given y1 = 0.33 and P = 120 kPa, find x1 and T. (e) Given T = 105°C and P = 120 kPa, find x1 and y1. (f) For part (e), if the overall mole fraction of benzene is z1 = 0.33, what molar fraction of the two-phase system is vapor? (g) Why is Raoult's law likely to be an excellent VLE model for this system at the stated (or computed) conditions?

          Assuming the validity of Raoult's law, do the following calculations for the benzene(1) / toluene(2) system:
(a) Given x1 = 0.33 and T = 100°C, find y1 and P.
(b) Given y1 = 0.33 and T = 100°C, find x1 and P.
(c) Given x1 = 0.33 and P = 120 kPa, find y1 and T.
(d) Given y1 = 0.33 and P = 120 kPa, find x1 and T.
(e) Given T = 105°C and P = 120 kPa, find x1 and y1.
(f) For part (e), if the overall mole fraction of benzene is z1 = 0.33, what molar fraction of the two-phase system is vapor?
(g) Why is Raoult's law likely to be an excellent VLE model for this system at the stated (or computed) conditions?

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