23-Chem-A1 Process Balances and Chemical Thermodynamics · December 2013
Question 1 of 7: Acetone Evaporated into Nitrogen and Compressed
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exams — December 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. Property data needed (densities, molar masses, steam-table and thermochemical values) 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, humidity and gas laws; Smith, Van Ness, Abbott & Swihart, Introduction to Chemical Engineering Thermodynamics (8th ed., McGraw-Hill) — excess properties, VLE, residual properties and reaction equilibrium; supporting property data from Perry's Chemical Engineers' Handbook (9th ed.), the NIST/ASME steam tables and the NIST Chemistry WebBook.
Question 1: Acetone Evaporated into Nitrogen and Compressed (equal value)
Given. Liquid acetone 400 L/min evaporated into N₂, then a second N₂ stream of 419 m³(STP)/min dilutes it; the mixture is compressed to 7.3 atm and 325 °C with acetone partial pressure 501 mm Hg. Property data (open-book): acetone density $\rho = 0.791$ g/mL and molar mass $M = 58.08$ g/mol; standard molar volume 22.414 L/mol at STP (0 °C, 1 atm).
Stream / datum
Value
Liquid acetone fed
400 L/min
Second N₂ (dilution)
419 m³(STP)/min
Final total pressure
7.3 atm = 5548 mm Hg
Acetone partial pressure (final)
501 mm Hg
Find. (a) the mole-fraction composition of the compressed stream; (b) the volumetric flow rate of the N₂ that enters the evaporator, evaluated at 27 °C and 1235 mm Hg.
Figure 1 — Acetone evaporates into nitrogen, is diluted by a second N₂ stream, then compressed. Acetone is conserved through the train.
Approach. Convert the liquid acetone to a molar flow, use the acetone partial-pressure ratio to fix the mole fractions and the total molar flow, then split the nitrogen between the two N₂ feeds and apply the ideal-gas law to the evaporator N₂ at the stated conditions.
Molar flow of acetone fed. The liquid rate times density over molar mass gives the moles evaporated (all of it ends up in the gas):
$$\dot n_a = \frac{(400\ \text{L/min})(791\ \text{g/L})}{58.08\ \text{g/mol}} = \boxed{5447.7\ \text{mol/min}}.$$
Mole fraction of acetone in the product. By Dalton's law the acetone mole fraction equals its partial-pressure ratio at the compressor outlet ($P_{tot}=7.3\times760=5548$ mm Hg):
$$y_a = \frac{p_a}{P_{tot}} = \frac{501}{5548} = 0.0903 \;\Rightarrow\; \boxed{9.03\%\ \text{acetone},\ 90.97\%\ \text{N}_2}.$$
That is part (a).
Total and nitrogen molar flows. Since acetone is 9.03 % of the total, the total molar flow and the total nitrogen follow:
$$\dot n_{tot} = \frac{\dot n_a}{y_a} = \frac{5447.7}{0.0903} = 60{,}327\ \text{mol/min},\qquad \dot n_{\text{N}_2} = 60{,}327-5447.7 = 54{,}879\ \text{mol/min}.$$
Split the nitrogen between the two feeds. The dilution stream is 419 m³ at STP:
$$\dot n_{\text{N}_2,\text{dil}} = \frac{419{,}000\ \text{L/min}}{22.414\ \text{L/mol}} = 18{,}694\ \text{mol/min},$$
so the nitrogen entering the evaporator is the difference,
$$\dot n_{\text{N}_2,\text{evap}} = 54{,}879 - 18{,}694 = 36{,}185\ \text{mol/min}.$$
Volumetric flow of the evaporator nitrogen. Apply the ideal-gas law at $T=300.15$ K and $P=1235$ mm Hg $=1.625$ atm:
$$\dot V = \frac{\dot n_{\text{N}_2,\text{evap}} R T}{P} = \frac{(36{,}185)(0.08206)(300.15)}{1.625} = 5.48\times10^{5}\ \text{L/min} = \boxed{548\ \text{m}^3/\text{min}}.$$
That is part (b).