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.
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.)
Stoichiometric oxygen and air. $$n_{\text{O}_2} = 8\times13{,}860 = 110{,}880\ \text{mol}, \qquad n_{\text{air}} = \frac{n_{\text{O}_2}}{0.21} = \frac{110{,}880}{0.21} = \boxed{528{,}000\ \text{mol air}}$$
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
Quantity
Value
Fuel moles
13,860 mol
Stoichiometric O2
110,880 mol
Air required
528,000 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.