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18-Env-B5 Industrial & Hazardous Waste Management · December 2019

Question 8 of 10: Combustion Air for One Tonne of Organic Solid Waste (C 5 H 12 )

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

Notes on this paper

Reference texts: LaGrega, Buckingham & Evans, Hazardous Waste Management, 2nd ed.; Nemerow & Dasgupta, Industrial and Hazardous Waste Treatment, 2nd ed.; Davis & Cornwell, Introduction to Environmental Engineering, 6th ed.; Metcalf & Eddy, Wastewater Engineering: Treatment and Resource Recovery, 5th ed.; Cooper & Alley, Air Pollution Control: A Design Approach; ACGIH, Industrial Ventilation: A Manual of Recommended Practice; Ontario Environmental Protection Act, R.S.O. 1990, c. E.19 and O. Reg. 347 (Waste Management – General); U.S. EPA SW-846 Method 1311 (Toxicity Characteristic Leaching Procedure).

Question 8: Combustion Air for One Tonne of Organic Solid Waste (C5H12) (10 marks)

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. Fuel: $\text{C}_5\text{H}_{12}$, mass $= 1\ \text{tonne} = 1{,}000{,}000\ \text{g}$. Air composition assumed 21% O2 / 79% N2 by volume (standard atmospheric air).

Find. The mass (and volume, at STP) of air required for stoichiometric complete combustion.

Approach. Balance the combustion equation, convert the fuel mass to moles, scale to stoichiometric O2, then divide by the 21% O2 mole fraction of air to get the total air requirement.

  1. Balance the combustion equation. Complete combustion of a hydrocarbon produces only CO2 and H2O: $$\text{C}_5\text{H}_{12}+8\text{O}_2\longrightarrow5\text{CO}_2+6\text{H}_2\text{O}$$ (Carbon: $5=5$; Hydrogen: $12=12$; Oxygen: $8\times2=16=5\times2+6\times1$ — balanced.)
  2. Moles of fuel. $M_{\text{C}_5\text{H}_{12}} = 5(12.011)+12(1.008) = 72.15\ \text{g/mol}$: $$n_{\text{fuel}} = \frac{1{,}000{,}000\ \text{g}}{72.15\ \text{g/mol}} = \boxed{13{,}860\ \text{mol}}$$
  3. Stoichiometric oxygen and air. $$n_{\text{O}_2} = 8\times13{,}860 = 110{,}880\ \text{mol}, \qquad n_{\text{air}} = \frac{n_{\text{O}_2}}{0.21} = \frac{110{,}880}{0.21} = \boxed{528{,}000\ \text{mol air}}$$
  4. Convert to mass and volume. Using $M_{\text{air}}\approx28.97\ \text{g/mol}$ and the molar volume at STP ($22.4\ \text{L/mol}$): $$m_{\text{air}} = 528{,}000\times28.97 = 1.530\times10^{7}\ \text{g} = \boxed{15{,}300\ \text{kg}} \approx 15.3\ \text{tonnes}$$ $$V_{\text{air}} = 528{,}000\times22.4\ \text{L/mol} = \boxed{1.18\times10^{7}\ \text{L}}\approx11{,}830\ \text{m}^3\ \text{(STP)}$$
Final results
QuantityValue
Fuel moles13,860 mol
Stoichiometric O2110,880 mol
Air required528,000 mol $\approx$ 15,300 kg (15.3 tonnes) $\approx$ 11,830 m³ at STP
Check: the printed formula $\text{C}_5\text{H}_{12}$ (pentane) is used literally as the exam gives it, despite the question describing it as "organic solid waste" — pentane is a liquid/gas at ambient conditions, so this is a simplified elemental surrogate for the waste's C:H ratio rather than a literal material identification, consistent with how such stoichiometric-air problems are typically posed. This is stoichiometric (theoretical) air only; a real incinerator would run with 20–50% excess air for complete combustion assurance, which is not requested here.