23-Chem-A1 Process Balances and Chemical Thermodynamics · Undated paper
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
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.
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):
| Species | Mass (g) | $M$ (g/mol) | $n_i$ (mol) | $y_i$ | $a_i$ (L²bar/mol²) | $b_i$ (L/mol) |
|---|---|---|---|---|---|---|
| H₂ | 70.40 | 2.016 | 34.92 | 0.7872 | 0.2331 | 0.02580 |
| CH₄ | 23.68 | 16.043 | 1.476 | 0.0333 | 2.303 | 0.04306 |
| C₂H₄ | 35.84 | 28.054 | 1.278 | 0.0288 | 4.611 | 0.05821 |
| CO₂ | 66.00 | 44.01 | 1.500 | 0.0338 | 3.657 | 0.04285 |
| CO | 94.92 | 28.01 | 3.389 | 0.0764 | 1.472 | 0.03948 |
| N₂ | 50.40 | 28.014 | 1.799 | 0.0406 | 1.384 | 0.03886 |
| Total | 44.36 mol | 78.7 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.
| Quantity | Result |
|---|---|
| Total moles | 44.36 mol |
| (a) Ideal-gas volume | 712.9 L (0.713 m³) |
| $a_{mix}$ / $b_{mix}$ | 0.4864 L²bar/mol² / 0.02946 L/mol |
| (b) van der Waals volume | 713.9 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.