13.1 Assuming the validity of Raoult's law, do the following calculations for the ben- zene(1)/toluene(2) system: (a) Given x₁ = 0.33 and T = 100°C, find y₁ and P. (b) Given yı = 0.33 and T = 100°C, find x₁ and P.

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13.1 Assuming the validity of Raoult's law, do the following calculations for the ben-
zene(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°℃, 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 frac-
tion 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?
Transcribed Image Text:13.1 Assuming the validity of Raoult's law, do the following calculations for the ben- zene(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°℃, 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 frac- tion 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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