23-Chem-A1 Process Balances and Chemical Thermodynamics · May 2013
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
National Exams — May 2013 — 04-Chem-A1 Process Balances and Chemical Thermodynamics. Three-hour, open-book exam; any non-communicating calculator permitted. Format: seven questions in three parts — answer one of Q1–Q2 (Part A), one of Q3–Q4 (Part B) and two of Q5–Q7 (Part C); four questions of equal value constitute a complete paper. All seven are solved below for completeness. Where property data are needed they are stated explicitly in each Given block. Units follow the paper (mixed SI and US customary).
Reference texts: Felder, Rousseau & Bullard, Elementary Principles of Chemical Processes (4th ed., Wiley) — material & energy balances; Smith, Van Ness, Abbott & Swihart, Introduction to Chemical Engineering Thermodynamics (8th ed., McGraw-Hill) — VLE, residual properties, reaction equilibrium; supporting data from Perry's Chemical Engineers' Handbook (9th ed.) and the NIST Chemistry WebBook.
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. Overhead vapour $V$ (95.0% methanol) is condensed into the accumulator. Over the 12-h test: product to storage $P=7500$ lbm; reflux $R=0.80\,V$; drum level fell by 3.5 in at 50 gal/in; the drum liquid is the 95% methanol condensate. Density of the condensate is taken as that of methanol, $\rho\approx 0.792\ \text{g/mL} = 6.61\ \text{lb/gal}$ (property data, open-book).
Find. The mass of methanol condensed during the test (i.e. the methanol content of the total condensed vapour $V$).
Approach. Write an unsteady total mass balance on the accumulator drum over the test — condensed vapour in, reflux and product out, and the measured inventory change — then convert $V$ to methanol using the 95% purity.
| Quantity | Result |
|---|---|
| Inventory change (level drop) | $-175$ gal $\approx -1157$ lbm |
| Total vapour condensed, $V$ | $\approx 31{,}700$ lbm |
| Methanol condensed | $\approx 3.01\times10^{4}$ lbm (≈ 30,100 lbm) |
Check: the condensate density is taken as pure-methanol (6.61 lb/gal); at 95 wt% methanol and the drum temperature it may run 1–3% higher, shifting the inventory term by only ≈ ±30 lbm and $V$ by ≈ ±150 lbm (<0.5%). The 5 psig drum pressure is not needed for the liquid balance.