23-Chem-A1 Process Balances and Chemical Thermodynamics · December 2016
Question 2 of 6: Combustion of Wood by Orsat Analysis
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exams — December 2016 — 04-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 masses, critical constants, acentric factors, Rackett Zc) 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) — material balances, combustion/Orsat analysis, humidity; Himmelblau & Riggs, Basic Principles and Calculations in Chemical Engineering (8th ed.) — heats of reaction and Kirchhoff’s law; Smith, Van Ness, Abbott & Swihart, Introduction to Chemical Engineering Thermodynamics (8th ed., McGraw-Hill) — fugacity, generalized virial correlations, reaction equilibrium and VLE; supporting property data from Perry’s Chemical Engineers’ Handbook (9th ed.) and the NIST Chemistry WebBook.
Question 2: Combustion of Wood by Orsat Analysis (Part A — equal value)
Given. Wood (mass %): C 45.9, O 23.1, ash 5.1, and moisture + combustible H making up the remaining 25.9%. Dry (Orsat) flue gas mol%: CO₂ 14.8, CO 1.66, O₂ 3.46, N₂ 80.08. Air is 21% O₂ / 79% N₂. Molar masses: C 12.01, O 16.00, H 1.008, N₂ 28.01, O₂ 32.00, H₂O 18.02.
Find. (a) full ultimate analysis (split moisture from H); (b) fuel/air mass ratio; (c) % excess air; (d) wet flue-gas composition.
Approach. Take 100 mol dry flue gas as basis. The nitrogen is the tie to air; the carbon (CO₂+CO) ties to the wood mass; an oxygen-atom balance — written so the free-moisture oxygen cancels — isolates the combustible hydrogen, after which moisture follows by difference.
Basis and the carbon tie. Basis: 100 mol dry flue gas. Carbon in the flue $=14.8+1.66=16.46$ mol. Since the wood is 45.9% C, the wood mass per 100 mol flue is
$$M_{\text{wood}}=\frac{16.46\times12.01}{0.459}=430.7\ \text{g}.$$
Hence wood O atoms $=0.231(430.7)/16.00=6.219$ mol, and moisture + H mass $=0.259(430.7)=111.6$ g.
Air from the nitrogen tie. All N₂ comes from air, so O₂ supplied is
$$\dot n_{\text{O}_2,\text{air}}=80.08\times\frac{21}{79}=21.29\ \text{mol}.$$
Oxygen-atom balance → combustible H. Let $h$ = mol H atoms in the fuel; the free moisture enters and leaves as the same H₂O, so its oxygen cancels. Balancing O atoms (air + wood O = CO₂ + CO + flue O₂ + combustion water):
$$2(21.29)+6.219 = 2(14.8)+1.66+2(3.46)+\tfrac{h}{2}\;\Rightarrow\; h = 21.23\ \text{mol H}.$$
So combustible H $=21.23\times1.008=21.4$ g $\Rightarrow \boxed{4.97\%\ \text{H}}$, and moisture $=111.6-21.4=90.2$ g $\Rightarrow \boxed{20.93\%\ \text{moisture}}$.
Complete analysis (part a). C 45.9%, O 23.1%, ash 5.1%, H 4.97%, moisture 20.93% (sums to 100%).
Fuel-to-air ratio (part b). Air mass $=80.08(28.01)+21.29(32.00)=2924$ g per 100 mol flue:
$$\frac{\text{fuel}}{\text{air}}=\frac{430.7}{2924}=\boxed{0.147\ \text{kg fuel/kg air}}\quad(\text{air/fuel}=6.79).$$
Excess air (part c). Theoretical O₂ for complete combustion of the fuel fed (all C→CO₂, all H→H₂O), crediting the wood’s own oxygen:
$$\dot n_{\text{O}_2,\text{theo}}=16.46+\tfrac{h}{4}-\tfrac{6.219}{2}=16.46+5.305-3.109=18.66\ \text{mol},$$
$$\%\,\text{excess}=\frac{21.29-18.66}{18.66}\times100=\boxed{14.1\%}.$$
Wet flue-gas composition (part d). Total water $=\tfrac{h}{2}+\text{moisture}=10.61+5.005=15.62$ mol, so wet total $=115.62$ mol:
$$\text{CO}_2\ 12.80\%,\ \ \text{CO}\ 1.44\%,\ \ \text{O}_2\ 2.99\%,\ \ \text{N}_2\ 69.26\%,\ \ \text{H}_2\text{O}\ 13.51\%.$$
Quantity
Result
(a) Wood analysis
C 45.9, O 23.1, ash 5.1, H 4.97, moisture 20.93 (wt%)