Chemical synthesis · Lesson 2
How much can we make?
The mole map, limiting and excess reagents, theoretical and percentage yield, and gases at industrial conditions.
A fertiliser plant runs on a balance sheet written in moles. Every tonne of ammonia sold starts as nitrogen and hydrogen bought, compressed and heated, and the company needs to know three numbers: which raw material runs out first, how much product is possible, and how much it actually gets. Those are the limiting reagent, the theoretical yield and the percentage yield.
The mole map
Every calculation goes through moles: n = m ÷ M for solids and liquids, n = cV for solutions (V in litres), n = V ÷ 22.71 for gases at STP (0.0 °C and 100.0 kPa), and n = PV ÷ RT for gases at any other conditions, with P in kPa, V in L, T in kelvin and R = 8.314 J K⁻¹ mol⁻¹.
Limiting and excess reagents
The limiting reagent is the reactant that runs out first; it fixes how much product can form. The other reactant is in excess. You cannot tell which is limiting from the masses: convert to moles and compare with the equation’s ratio. 10.0 g of N₂ (0.357 mol) needs 1.07 mol of H₂, so 3.00 g of H₂ (1.49 mol) is in excess even though its mass is smaller.
Try it with a real experiment: magnesium ribbon dropped into hydrochloric acid, with the hydrogen collected in a gas syringe. Change the amounts and see which reagent limits the volume.
Notice that once magnesium is limiting, adding more acid does not produce more gas; it only makes the reaction faster.
Theoretical and percentage yield
The theoretical yield is the maximum amount of product, calculated from the limiting reagent. The percentage yield = actual ÷ theoretical × 100. Yields fall below 100% because reactions may be reversible, side reactions form other products, and product is lost when it is filtered, washed, recrystallised or transferred. In a synthesis with several steps, the overall yield is the product of the step yields: 85% × 70% × 60% is only 35.7%.
Gases at industrial conditions
Industrial gases are rarely at STP. Roasting 2.20 tonnes of zinc sulfide with a 72.0% yield gives 1.625 × 10⁴ mol of SO₂; at 300.0 °C (573.15 K) and 165.0 kPa this occupies V = nRT ÷ P = 4.69 × 10⁵ L. The answer is given to 3 significant figures because the least precise data (2.20 t, 72.0%) have 3.
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