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23-Chem-B6 Petroleum Refining and Petrochemicals · May 2018

Question 5 of 5: Vapour–liquid equilibrium: Raoult's vs Henry's law

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

National Exam 16-Chem-B6, Petroleum Refining and Petrochemicals — May 2018. 3 hours, OPEN BOOK (any non-communicating calculator permitted). Per the exam notes, FIVE (5) questions constitute a complete paper and each is of equal value (10 marks); Questions 1–3 require essay-format answers where clarity and organisation are marked, while Questions 4 and 5 (and the material balance in 2b) are quantitative. This paper contains exactly five questions, so all five are answered here in full.

Reference texts: Gary, Handwerk & Kaiser, Petroleum Refining: Technology and Economics, 5th ed. (CRC, 2007); Fahim, Al-Sahhaf & Elkilani, Fundamentals of Petroleum Refining (Elsevier, 2010); J. G. Speight, The Chemistry and Technology of Petroleum, 5th ed.; Smith, Van Ness & Abbott, Introduction to Chemical Engineering Thermodynamics, 8th ed. (VLE, Raoult/Henry); Felder & Rousseau, Elementary Principles of Chemical Processes, 4th ed. (material balances).

Question 5 — Vapour–liquid equilibrium: Raoult's vs Henry's law (10 marks)

Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.

(a) Benzene–toluene — Raoult's law

Given. $x_B=x_T=0.5$ at $T=30\ \text{°C}$; Antoine constants as tabulated.

Find. System pressure $P$ and vapour composition $y_B,\,y_T$.

Why Raoult. Benzene and toluene are chemically very similar, adjacent aromatics that form a nearly ideal liquid solution over the whole composition range; both are present at high (50%) concentration. Raoult's law, $p_i=x_iP_i^{sat}$, is therefore the appropriate model.

  1. Pure-component vapour pressures at 30 °C (Antoine). $$\log_{10}P_B^{sat}=6.906-\frac{1211}{30+220.8}=2.077\ \Rightarrow\ P_B^{sat}=119.5\ \text{mmHg},$$ $$\log_{10}P_T^{sat}=6.953-\frac{1343.9}{30+219.4}=1.565\ \Rightarrow\ P_T^{sat}=36.7\ \text{mmHg}.$$
  2. System pressure by Raoult's law. The total pressure is the sum of partial pressures: $$P=x_BP_B^{sat}+x_TP_T^{sat}=0.5(119.5)+0.5(36.7)=\boxed{78.1\ \text{mmHg}}\;(0.103\ \text{atm}).$$
  3. Vapour composition (Dalton). $$y_B=\frac{x_BP_B^{sat}}{P}=\frac{59.75}{78.1}=\boxed{0.765},\qquad y_T=1-y_B=0.235.$$ The vapour is enriched in the more volatile benzene ($y_B>x_B$), as expected.

(b) Ethane in water — Henry's law

Given. Gas at $P=20\ \text{atm}$ with $y_{\text{eth}}=0.010$; water at 20 °C; $H_{\text{eth}}=2.63\times10^{4}\ \text{atm/mole fraction}$.

Find. Mole fraction of ethane dissolved in the water, $x_{\text{eth}}$.

Why Henry. Ethane is a light, essentially non-condensable gas that is only sparingly soluble in water; it exists at very low mole fraction in the liquid, the regime where Henry's law $p_i=H_i x_i$ applies. (Raoult's law is invalid here — ethane has no meaningful liquid-phase vapour pressure at 20 °C, and water/ethane are grossly dissimilar.)

  1. Partial pressure of ethane in the gas (Dalton). $$p_{\text{eth}}=y_{\text{eth}}P=0.010\times20=0.20\ \text{atm}.$$
  2. Dissolved mole fraction from Henry's law. $$x_{\text{eth}}=\frac{p_{\text{eth}}}{H_{\text{eth}}}=\frac{0.20}{2.63\times10^{4}} =\boxed{7.6\times10^{-6}}.$$ The dissolved ethane is minute — consistent with the sparing solubility that justified Henry's law.
QuantityValue
(a) $P_B^{sat}$, $P_T^{sat}$ at 30 °C119.5, 36.7 mmHg
(a) System pressure $P$78.1 mmHg (0.103 atm)
(a) Vapour composition $y_B / y_T$0.765 / 0.235
(b) Ethane partial pressure0.20 atm
(b) Dissolved ethane $x_{\text{eth}}$$7.6\times10^{-6}$

(The benzene and toluene Henry constants quoted in the exam are not used: at these high liquid concentrations Raoult's law, not Henry's law, is the correct model for part a.)

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