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23-Chem-A1 Process Balances and Chemical Thermodynamics · December 2017

Question 5 of 6: Isomerization Equilibrium and a Dew Point

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

Notes on this paper

National Exams — December 2017 — 16-Chem-A1 Process Balances and Chemical Thermodynamics. Three-hour, open-book exam; any non-communicating calculator permitted. Format: two parts — Part A (Q1–Q3) Process Balances, Part B (Q4–Q6) Chemical Thermodynamics; the candidate answers two questions from each part (four constitute a complete paper, equal value). All six questions are solved below for completeness. Property data not printed on the paper (molar volumes at STP, gas constant, Rankine conversion) are stated explicitly in each Given block as open-book look-ups.

Reference texts: Felder, Rousseau & Bullard, Elementary Principles of Chemical Processes (4th ed., Wiley) — recycle balances, humidity and adiabatic-flame (energy) balances; Himmelblau & Riggs, Basic Principles and Calculations in Chemical Engineering (8th ed.) — multi-unit separation balances; Smith, Van Ness, Abbott & Swihart, Introduction to Chemical Engineering Thermodynamics (8th ed., McGraw-Hill) — cubic equations of state, residual properties, reaction/phase equilibrium and gas-cycle work; supporting property data from Perry’s Chemical Engineers’ Handbook (9th ed.).

Question 5: Isomerization Equilibrium and a Dew Point (Part B — equal value)

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.

Given. $T=400$ K; vapour pressures $P_A^{\text{sat}}=2$ atm, $P_B^{\text{sat}}=2.5$ atm; the gas is always at reaction equilibrium ($y_B/y_A$ constant, independent of $P$ for an equimolar isomerization); first liquid (dew point) appears at $P=2.2$ atm; ideal liquid solution (Raoult’s law, $\gamma_i=1$).

Find. (a) $K_g=a_B/a_A$ for the gas reaction; (b) $K_l=a_B/a_A$ for the liquid reaction.

Approach. At the dew point the vapour composition equals the overall (equilibrium) gas composition, and the incipient liquid satisfies Raoult’s law; the constraint $x_A+x_B=1$ fixes the vapour composition, hence both equilibrium constants.

  1. Dew-point (Raoult) relations. The incipient liquid mole fractions are $x_A=y_AP/P_A^{\text{sat}}$ and $x_B=y_BP/P_B^{\text{sat}}$. Requiring $x_A+x_B=1$ at $P=2.2$ atm: $$y_A\frac{2.2}{2.0}+y_B\frac{2.2}{2.5}=1\;\Rightarrow\;1.10\,y_A+0.88\,y_B=1.$$
  2. Solve for the vapour composition. With $y_A+y_B=1$: $1.10y_A+0.88(1-y_A)=1\Rightarrow0.22y_A=0.12$, so $$y_A=0.545,\qquad y_B=0.455.$$
  3. Gas-phase equilibrium constant (part a). For A(g)↔B(g) with ideal gases, $K_g=(p_B/P^\circ)/(p_A/P^\circ)=y_B/y_A$: $$K_g=\frac{0.455}{0.545}=\boxed{0.833}.$$
  4. Incipient-liquid composition. From Raoult at the dew point: $$x_A=y_A\frac{P}{P_A^{\text{sat}}}=0.545\frac{2.2}{2.0}=0.600,\qquad x_B=y_B\frac{P}{P_B^{\text{sat}}}=0.455\frac{2.2}{2.5}=0.400\;(x_A+x_B=1).$$
  5. Liquid-phase equilibrium constant (part b). For A(l)↔B(l) with ideal solutions ($\gamma=1$), $K_l=x_B/x_A$: $$K_l=\frac{0.400}{0.600}=\boxed{0.667}.$$ Consistently, $K_l=K_g\,(P_A^{\text{sat}}/P_B^{\text{sat}})=0.833(2.0/2.5)=0.667$, the thermodynamic link between the gas- and liquid-phase constants through the pure-component vapour pressures.
QuantityResult
Vapour composition at dew point$y_A=0.545,\ y_B=0.455$
Incipient-liquid composition$x_A=0.600,\ x_B=0.400$
(a) $K_g$ for A(g)↔B(g)0.833
(b) $K_l$ for A(l)↔B(l)0.667