Chemistry • Year 11 • Module 2 • Lesson 14

Percentage Yield & Percentage Purity

Apply purity and yield calculations to real industrial data, interpret graphs, compare processes, and practise the full purity–stoichiometry–yield sequence.

Apply · Data & Reasoning

1. Interpret industrial process data

A chemical plant runs three reactions. The table below records the key data for each. 9 marks

Reaction Reactant sample (g) % purity of sample Theoretical yield (g) Actual yield (g) % yield
A: CaCO3 → CaO + CO2 50.0 90.0% calculate 22.7
B: Fe2O3 + 3CO → 2Fe + 3CO2 100.0 80.0% calculate 38.0
C: Mg + 2HCl → MgCl2 + H2 25.0 100% (pure) calculate 91.5

Molar masses: Ca=40.078, C=12.011, O=15.999, Fe=55.845, Mg=24.305, Cl=35.453.

1.1 For Reaction A: apply the purity correction, then complete the four-step stoichiometry to find the theoretical yield of CaO. Then calculate % yield. Show full working. 3 marks

1.2 For Reaction B: apply purity, complete stoichiometry, find theoretical yield of Fe, then calculate % yield. 3 marks

1.3 For Reaction C (pure Mg): calculate theoretical yield of MgCl2, then calculate % yield. 2 marks

1.4 Which reaction has the highest percentage yield? Suggest one reason why. 1 mark

Stuck? For each: m(pure) = m(sample) × (% purity ÷ 100); then n = m(pure) ÷ MM; apply mole ratio; m(product) = n × MM(product). Then % yield = actual ÷ theoretical × 100.

2. Interpret a yield vs temperature graph — contact process

The graph below shows the equilibrium percentage yield of SO3 in the contact process (2SO2 + O2 ⇄ 2SO3) plotted against temperature at a fixed pressure. The industrial operating temperature is marked. 7 marks

0 20 40 60 80 100 400 450 500 550 600 650 700 Temperature (°C) Equilibrium % yield of SO₃ Industrial: 450 °C

Figure 2. Equilibrium % yield of SO3 from 2SO2 + O2 ⇄ 2SO3 as a function of temperature at constant pressure. Illustrative data based on industrial contact-process parameters.

2.1 Describe the trend shown in the graph. 2 marks

2.2 Read the approximate equilibrium yield at 450 °C. Then calculate the actual mass of SO3 expected from 100 g of pure SO2 reacting at 450 °C. (S=32.06, O=15.999) 3 marks

2.3 The Contact Process reaction is reversible: 2SO2 + O2 ⇄ 2SO3. A student claims: “The graph shows we can never achieve 100% yield even at 400 °C.” Using your knowledge of reversible reactions from the lesson, explain why the equilibrium % yield is less than 100% at all temperatures, and state what the graph tells you about how temperature affects the equilibrium position for this reaction. 2 marks

Stuck? For 2.2: n(SO2) = 100 ÷ 64.058; ratio SO2:SO3 = 1:1; m(theoretical) = n × MM(SO3); actual = theoretical × (% yield ÷ 100).

3. Predict and justify — the Haber process for ammonia

The Haber process: N2(g) + 3H2(g) ⇄ 2NH3(g). A chemical plant uses a 90.0% pure N2 feed (contaminated with Ar gas) and achieves a 25.0% yield per pass through the reactor. The plant starts with 56.0 kg of N2 feed. 6 marks

3.1 Calculate the mass of pure N2 available. Then calculate the theoretical yield of NH3. Then calculate the actual yield of NH3 per pass. Show the full sequence. (N=14.007, H=1.008) 4 marks

3.2 Predict what would happen to the actual yield per pass if the purity of the N2 feed were improved to 99.0% while the % yield remained 25.0%. Justify your prediction with a calculation. 2 marks

Stuck? Sequence: m(pure N2) = 56 000 × 0.900 → n(N2) → ratio 1:2 → n(NH3) → theoretical m(NH3) → actual = theoretical × 0.250.

4. Compare percentage purity and percentage yield across five features

Complete the two-column table. For each feature, write a concise description that contrasts the two corrections. 10 marks (1 per cell)

FeaturePercentage purityPercentage yield
What it measures
Applied to reactant or product?
When to apply it in the calculation sequence
Formula
Australian context example
Stuck? Revisit the “When to Apply Each Correction” section and the copy-into-your-books grid in the lesson.
Answers — Do not peek before attempting

Q1.1 — Reaction A: CaCO3 → CaO (3 marks)

m(pure CaCO3) = 50.0 × 0.900 = 45.0 g. n(CaCO3) = 45.0 ÷ 100.09 = 0.4496 mol. Ratio 1:1; n(CaO) = 0.4496 mol. MM(CaO) = 56.077; theoretical m(CaO) = 0.4496 × 56.077 = 25.2 g. % yield = (22.7 ÷ 25.2) × 100 = 90.1%. [1 purity, 1 stoichiometry, 1 % yield]

Q1.2 — Reaction B: Fe2O3 → Fe (3 marks)

m(pure Fe2O3) = 100.0 × 0.800 = 80.0 g. MM(Fe2O3) = 159.69; n = 80.0 ÷ 159.69 = 0.5010 mol. Ratio 1:2; n(Fe) = 1.002 mol. MM(Fe) = 55.845; theoretical = 1.002 × 55.845 = 55.9 g. % yield = (38.0 ÷ 55.9) × 100 = 68.0%. [1 purity, 1 stoichiometry, 1 % yield]

Q1.3 — Reaction C: Mg → MgCl2 (2 marks)

n(Mg) = 25.0 ÷ 24.305 = 1.028 mol. Ratio 1:1; n(MgCl2) = 1.028 mol. MM(MgCl2) = 95.211; theoretical = 1.028 × 95.211 = 97.9 g. % yield = (91.5 ÷ 97.9) × 100 = 93.5%. [1 stoichiometry, 1 % yield]

Q1.4 — Highest yield (1 mark)

Reaction C (93.5%). Possible reason: pure reactant means no moles are diverted to impurity reactions; the reaction (metal + acid) may also proceed with few side reactions under controlled conditions.

Q2.1 — Graph trend (2 marks)

As temperature increases from 400 °C to 700 °C, the equilibrium % yield of SO3 decreases from approximately 99% to 35% [trend]. The decrease is approximately linear over this range, with yield falling by about 2% per 10 °C rise [shape/rate detail].

Q2.2 — Actual yield at 450 °C (3 marks)

Reading: % yield at 450 °C ≈ 97%. n(SO2) = 100 ÷ 64.058 = 1.561 mol. Ratio SO2:SO3 = 1:1; n(SO3) = 1.561 mol. MM(SO3) = 80.057; theoretical m(SO3) = 1.561 × 80.057 = 124.9 g. Actual = 124.9 × (97 ÷ 100) = 121.2 g. [1 read, 1 theoretical, 1 actual]

Q2.3 — Reversible reactions and equilibrium yield (2 marks)

A reversible reaction reaches equilibrium before all the reactants are consumed; at equilibrium, both forward and reverse reactions are occurring simultaneously, so the conversion is never complete and yield is always below 100% [1]. The graph shows that increasing temperature decreases the equilibrium % yield — meaning higher temperatures shift the equilibrium position towards the reactants (away from SO3), producing less product at equilibrium [1].

Q3.1 — Haber process full sequence (4 marks)

m(pure N2) = 56 000 × 0.900 = 50 400 g [P]. n(N2) = 50 400 ÷ 28.014 = 1799 mol [Step 2]. Ratio N2:NH3 = 1:2; n(NH3) = 3598 mol [Step 3]. MM(NH3) = 17.031; theoretical = 3598 × 17.031 = 61 293 g ≈ 61.3 kg [Step 4]. Actual = 61 293 × 0.250 = 15 323 g ≈ 15.3 kg per pass. [1 purity, 1 stoich, 1 theoretical, 1 actual]

Q3.2 — Effect of improved purity (2 marks)

Prediction: actual yield per pass increases because more pure N2 is available to react [1]. At 99.0% purity: m(pure) = 56 000 × 0.990 = 55 440 g; n(N2) = 1979 mol; n(NH3) = 3958 mol; theoretical = 67 433 g; actual = 67 433 × 0.250 = 16 858 g ≈ 16.9 kg — an increase of ~1.6 kg compared to 90% purity, confirming purity improvement raises output [1].

Q4 — Compare and contrast table

What it measures: Purity — the fraction of a reactant sample that is the desired substance. Yield — the efficiency of a reaction (how much product was obtained versus the maximum possible). Applied to reactant or product? Purity — reactant (starting material). Yield — product (what is collected at the end). When to apply: Purity — BEFORE stoichiometry (Step P, before Step 2). Yield — AFTER stoichiometry (once theoretical yield is known). Formula: Purity — % purity = (pure mass ÷ sample mass) × 100; rearranged: m(pure) = m(sample) × (% ÷ 100). Yield — % yield = (actual ÷ theoretical) × 100. Australian context example: Purity — iron ore at Port Kembla: ore may contain silicates and other minerals alongside Fe2O3; the percentage of Fe2O3 is the purity. Yield — the fraction of theoretical iron output actually tapped from the blast furnace; losses occur due to incomplete reduction and slag carryover.