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23-Chem-A1 Process Balances and Chemical Thermodynamics · Undated paper

Question 4 of 6: Part B — Chemical Thermodynamics

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

Notes on this paper

Reference texts: Felder, Rousseau & Bullard, Elementary Principles of Chemical Processes (4th ed., Wiley) — psychrometric (humidity) mass balances with recycle, fuel/air combustion stoichiometry, and waste-heat sensible-energy balances; Smith, Van Ness, Abbott & Swihart, Introduction to Chemical Engineering Thermodynamics (8th ed., McGraw-Hill) — the van der Waals equation of state with one-fluid mixing rules and the reaction-equilibrium constant from standard Gibbs energies; critical-property data from Poling, Prausnitz & O’Connell, The Properties of Gases and Liquids (5th ed.).

Paper structure. 16-CHEM-A1, May 2019, three hours, open book. Part A (Process Mass and Energy Balances) has three questions and Part B (Chemical Thermodynamics) has three. The printed numbering restarts at 1 in Part B, and the cover note reads “Part B (Questions 4 and 6)”. Candidates answer TWO questions from each part; four questions make a complete paper, each of equal value. All six questions are worked below, labelled A1–A3 and B1–B3.

Part A — Process Mass and Energy Balances

Part B — Chemical Thermodynamics

Question B1: Water Gas — Volume by Ideal-Gas and van der Waals Equations (25 points)

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. A six-component gas at $T=773.15$ K and $P=4$ bar, with the critical constants as printed. Masses are converted to moles with $n_i=m_i/M_i$, and $a_i=27R^2T_{c,i}^2/(64P_{c,i})$, $b_i=RT_{c,i}/(8P_{c,i})$ with $R=0.08314$ L·bar/(mol·K):

SpeciesMass (g)$M$ (g/mol)$n_i$ (mol)$y_i$$a_i$ (L²bar/mol²)$b_i$ (L/mol)
H₂70.402.01634.920.78720.23310.02580
CH₄23.6816.0431.4760.03332.3030.04306
C₂H₄35.8428.0541.2780.02884.6110.05821
CO₂66.0044.011.5000.03383.6570.04285
CO94.9228.013.3890.07641.4720.03948
N₂50.4028.0141.7990.04061.3840.03886
Total44.36 mol78.7 mol% H₂

Find. the gas volume (a) as an ideal gas and (b) from the van der Waals equation.

Approach. Sum the moles and get the ideal volume from $PV=nRT$. Then combine the pure-species van der Waals constants with the one-fluid mixing rules and solve the cubic for the molar volume.

  1. (a) Ideal-gas volume. $$V^{ig}=\frac{nRT}{P}=\frac{(44.36)(0.08314)(773.15)}{4}=\boxed{712.9\ \text{L}=0.713\ \text{m}^3}\qquad(V_m^{ig}=16.070\ \text{L/mol}).$$
  2. Mixing rules. With the classical van der Waals one-fluid rules, $$a_{mix}=\Big(\sum_i y_i\sqrt{a_i}\Big)^2=0.4864\ \text{L}^2\text{bar/mol}^2,\qquad b_{mix}=\sum_i y_i b_i=0.02946\ \text{L/mol}.$$
  3. (b) Solve the van der Waals cubic. Solve $\Big(P+\dfrac{a_{mix}}{V_m^2}\Big)(V_m-b_{mix})=RT$ with $RT=64.28$ L·bar/mol, starting from $V_m^{ig}=16.070$. Successive substitution in $V_m=b_{mix}+RT/(P+a_{mix}/V_m^2)$ converges in two passes to $$V_m=16.092\ \text{L/mol}\;\Rightarrow\;V^{vdW}=nV_m=(44.36)(16.092)=\boxed{713.9\ \text{L}=0.714\ \text{m}^3}.$$ Substituting back gives $(4+0.4864/16.092^2)(16.092-0.02946)=64.28$, so the root checks.
  4. Size of the correction. To first order, $V_m\approx RT/P+b_{mix}-a_{mix}/RT=16.070+0.0295-0.0076=16.092$ L/mol. The volume is +0.14% above ideal: the co-volume $b$ outweighs the attraction $a$ because the gas is far above every component's critical temperature.
QuantityResult
Total moles44.36 mol
(a) Ideal-gas volume712.9 L (0.713 m³)
$a_{mix}$ / $b_{mix}$0.4864 L²bar/mol² / 0.02946 L/mol
(b) van der Waals volume713.9 L (0.714 m³), +0.14% vs ideal

At 500 °C and 4 bar the reduced temperatures are all between 2.5 and 24 and the reduced pressures are below 0.31. At those conditions any real-gas equation should reproduce the ideal volume to within a fraction of a percent, and the van der Waals result does. A large correction here would signal an arithmetic error, not real-gas behaviour.