Chemistry • Year 12 • Module 6 • Lesson 4
Neutralisation in Everyday Life & Industry
Build HSC Band 5–6 extended-response technique on antacid chemistry, environmental neutralisation, and source critique.
1. Extended response — evaluate antacid options using patient data and chemistry (Band 5–6)
8 marks Band 5–6
Scenario + stimulus data
A clinical pharmacist at a Sydney hospital must recommend an antacid for a 68-year-old patient with the following conditions: (a) chronic acid reflux requiring twice-daily dosing; (b) stage 3 chronic kidney disease (reduced ability to excrete divalent cations Ca²⁺ and Mg²⁺); (c) severe constipation; (d) irritable bowel syndrome (IBS) that is aggravated by gas production. The pharmacist is choosing between the four antacids listed below.
| Antacid | Active ingredient | Reaction with HCl | Ion introduced | Bowel effect | CO₂ produced? |
|---|---|---|---|---|---|
| Option 1 | CaCO₃ | Acid + carbonate | Ca²⁺ | Constipating | Yes |
| Option 2 | Mg(OH)₂ | Acid + base | Mg²⁺ | Laxative | No |
| Option 3 | Al(OH)₃ | Acid + base | Al³⁺ | Constipating | No |
| Option 4 | NaHCO₃ | Acid + bicarbonate | Na⁺ | Neutral | Yes |
Q1. Evaluate each antacid option against the patient’s clinical criteria and recommend the most appropriate antacid. In your response you must:
- Write the balanced molecular equation for the recommended antacid reacting with HCl.
- Evaluate all four options against at least three of the patient’s criteria, explaining the chemistry behind each evaluation.
- Reach a clearly justified recommendation identifying which single antacid best satisfies the most criteria and why.
- Acknowledge any residual limitation of your recommended antacid that would require ongoing monitoring.
2. Source critique — evaluate a claim about flue gas desulfurisation (Band 5–6)
7 marks Band 5–6
“Flue gas desulfurisation is a complete solution to the problem of acid rain. Once scrubbers are installed, coal-fired power stations can operate indefinitely without any environmental impact from acid-forming gases. The scrubbing reaction Ca(OH)₂ + SO₃ → CaSO₄ + H₂O also produces a useful byproduct — gypsum (CaSO₄) — which can be sold to the construction industry to offset the full cost of the FGD system, making the technology self-funding.”
— Adapted from a fictional industry lobbying document, for worksheet purposes.
Q2. Evaluate this claim. Identify and explain three specific chemical or scientific errors in the passage and reformulate the claim into a scientifically accurate statement. In your response:
- For each error, clearly identify what is wrong and explain the correct chemistry.
- Write the correct balanced equation to replace any incorrect equation used in the source.
- Conclude with a reformulated claim that retains the useful information while correcting the errors.
3. Compare and evaluate — FGD vs direct acid rain remediation (Band 5–6)
7 marks Band 5–6
Context. A regional council in NSW is managing two consequences of sulfur dioxide emissions from a nearby industrial plant: (1) a lake with pH 4.3 (acidified by past acid rain) that now has no fish; (2) ongoing SO₂ emissions of 3000 ppm from the plant’s chimneys that risk further acidification. Engineers propose two strategies: Strategy A — install Ca(OH)₂ wet scrubbers on the plant chimneys (FGD); Strategy B — add powdered CaCO₃ directly to the lake to raise its pH and restore biodiversity.
Q3. Compare and evaluate both strategies for managing the environmental impact of SO₂ emissions in this scenario. In your response you must:
- Write balanced equations for the key neutralisation reaction in each strategy.
- Compare the two strategies on at least three criteria (e.g. speed, cost, scope of problem addressed, permanence, by-products, limitations).
- Explain whether Strategy A, Strategy B, or a combination is best for the council’s situation, justifying your answer with reference to both the lake and the ongoing SO₂ issue.
- Identify one limitation that neither strategy alone can address.
Q1 — Sample Band 6 response (8 marks), annotated
Evaluation of each option:
Option 1 (CaCO₃): Reaction: CaCO₃ + 2HCl → CaCl₂ + H₂O + CO₂. Fails criterion (b) — introduces Ca²⁺ ions which cannot be excreted by stage 3 CKD kidneys. Fails criterion (c) — constipating effect worsens existing constipation. Fails criterion (d) — produces CO₂ gas, exacerbating IBS. Not suitable (fails 3 criteria).
Option 2 (Mg(OH)₂): Reaction: Mg(OH)₂ + 2HCl → MgCl₂ + 2H₂O. Fails criterion (b) — introduces Mg²⁺ ions which cannot be excreted. Satisfies criterion (c) — laxative effect could actually relieve constipation. Satisfies criterion (d) — no CO₂. Partially suitable but kidney criterion is critical.
Option 3 (Al(OH)₃): Reaction: Al(OH)₃ + 3HCl → AlCl₃ + 3H₂O. Satisfies criterion (b) — introduces Al³⁺ not Ca²⁺/Mg²⁺. Fails criterion (c) — constipating effect worsens existing constipation. Satisfies criterion (d) — no CO₂. Partially suitable; 2 of 4 criteria met.
Option 4 (NaHCO₃): Reaction: NaHCO₃ + HCl → NaCl + H₂O + CO₂. Satisfies criterion (b) — introduces Na⁺ which is easily managed renally. Neutral bowel effect satisfies criterion (c). Fails criterion (d) — CO₂ produced exacerbates IBS. Disadvantage: lower efficacy per tablet. Partially suitable; 2 of 4 criteria met but CO₂ concern.
Recommendation: Option 3 (Al(OH)₃) is the best choice [1]. It is the only antacid that avoids Ca²⁺ and Mg²⁺ ion accumulation in a patient with reduced renal excretion (satisfies criterion (b), the most clinically critical) [1]. It produces no CO₂ (satisfies criterion (d)) [1]. The constipating effect (fails criterion (c)) can be managed by combining with a small dose of Mg(OH)₂ at physician discretion (a common clinical combination) [1].
Balanced equation: Al(OH)₃ + 3HCl → AlCl₃ + 3H₂O [1]. Reaction type: acid + base → salt + water. No CO₂ because Al(OH)₃ is a hydroxide base, not a carbonate [1].
Residual limitation: Long-term Al³⁺ accumulation in renal patients can itself cause toxicity (Al³⁺ deposits in bone and brain tissue — dialysis encephalopathy is a documented risk). Regular monitoring of serum aluminium levels would be required for chronic use [1]. Accept any biologically valid limitation specific to Al(OH)₃.
Marking criteria:
- 1 — Balanced equation for recommended antacid with HCl, correctly balanced.
- 1 — Identifies critical kidney criterion (no Ca²⁺/Mg²⁺) and eliminates Options 1 and 2 with chemical reasoning.
- 1 — Explains why CO₂ is/is not produced (carbonate vs hydroxide mechanism) for at least two options.
- 1 — Evaluates all four options against at least 3 criteria with chemistry-based reasoning.
- 1 — Clear recommendation with explicit justification citing the most clinically critical criterion.
- 1 — Acknowledges the bowel effect limitation and suggests how it could be managed.
- 1 — Acknowledges residual limitation of recommended antacid with specific mechanism.
- 1 — Overall response is structured, uses precise chemical terminology, and reaches a defensible recommendation that correctly weighs criteria hierarchically.
Q2 — Source critique: three errors (7 marks)
Error 1 — “Complete solution to acid rain.” This is incorrect. FGD removes 90–99% of SO₂ from flue gas, but it does not remove CO₂. CO₂ is the primary driver of ocean acidification and a major contributor to climate change (greenhouse effect). Additionally, FGD does not remediate lakes, soils, or ecosystems already acidified by past acid rain — it only prevents further SO₂ emissions at the treated source. It is a highly effective preventive measure, not a complete environmental solution [2 marks: 1 for identifying, 1 for correct explanation].
Error 2 — Wrong gas / wrong equation. The passage states the reaction as Ca(OH)₂ + SO₃ → CaSO₄ + H₂O. Two sub-errors: (a) The gas is SO₂ (sulfur dioxide — the primary combustion product of sulfur in coal), not SO₃ (sulfur trioxide). (b) The product of SO₂ with Ca(OH)₂ is CaSO₃ (calcium sulfite), not CaSO₄ (calcium sulfate / gypsum). Correct primary FGD equation: Ca(OH)₂(aq) + SO₂(g) → CaSO₃(s) + H₂O(l). Gypsum (CaSO₄) is obtained only by the separate oxidation step: 2CaSO₃ + O₂ → 2CaSO₄ [2 marks: 1 for correct gas + correct equation; 1 for explaining CaSO₃ vs CaSO₄ distinction].
Error 3 — Self-funding claim. While CaSO₄ (gypsum) does have commercial value in wallboard and cement manufacture, the sale of synthetic gypsum does not typically cover the full capital and operating costs of a large-scale FGD system. The claim that the system is “self-funding” overstates the economic benefit. Furthermore, gypsum is only produced after the additional oxidation step — the primary product of the FGD reaction is CaSO₃, which has fewer commercial uses [1 mark for identifying the overclaim; partial credit if student identifies only the CaSO₃/CaSO₄ distinction without the economic overclaim].
Reformulated claim: Flue gas desulfurisation is a highly effective technology for reducing SO₂ emissions from coal-fired power stations. In the primary reaction, Ca(OH)₂ neutralises SO₂ to produce CaSO₃(s), which can be further oxidised to CaSO₄ (gypsum) and sold to the construction industry, partially offsetting operating costs. Modern FGD systems remove 90–99% of SO₂ from flue gas. However, FGD does not remove CO₂ and cannot remediate ecosystems already damaged by acid rain; it should be considered one component of a broader environmental management approach rather than a complete solution [2 marks: 1 for a scientifically accurate reformulation that corrects all three errors; 1 for retaining accurate information while removing overclaims].
Q3 — Sample Band 6 response (7 marks), annotated
Key equations:
Strategy A (FGD): Ca(OH)₂(aq) + SO₂(g) → CaSO₃(s) + H₂O(l). Removes SO₂ at source before it forms acid rain [1 — correct equation].
Strategy B (lake liming): CaCO₃(s) + 2H⁺(aq) → Ca²⁺(aq) + H₂O(l) + CO₂(g). Neutralises existing acid in the lake [1 — correct equation].
Comparison on three criteria:
Scope: Strategy A addresses the source of the problem (prevents ongoing SO₂ release). Strategy B addresses a consequence (the already-acidified lake) but does nothing to prevent further SO₂ emissions — without Strategy A, the lake would re-acidify and require repeated treatment [1].
Permanence: Strategy A provides ongoing protection while the scrubber operates, removing 90–99% of SO₂. Strategy B provides a temporary pH correction — without addressing SO₂ source, the lake re-acidifies over time as more acid rain falls [1].
By-products and scale: Strategy A produces CaSO₃ (collectable solid, can be oxidised to gypsum for commercial use). Strategy B produces CO₂ gas (which escapes) and Ca²⁺ (remains in lake water as a harmless nutrient). Both by-products are benign at normal application rates [1].
Recommendation: A combination of both strategies is required [1]. Strategy A alone solves the ongoing SO₂ emission problem but does nothing to restore the lake’s current pH 4.3 to a level that supports fish (pH > 6.5 required). Strategy B alone temporarily raises lake pH, but without scrubbers the lake will re-acidify. Together: Strategy A prevents further acidification; Strategy B rehabilitates the existing ecosystem damage.
Limitation neither strategy addresses: Neither strategy addresses CO₂ emissions from the plant, which contribute to global ocean acidification and climate change through a separate chemical pathway. Broader decarbonisation (switching to renewables or carbon capture) would be required to address this limitation [1].
Marking criteria:
- 1 — Correct balanced equation for Strategy A (FGD with Ca(OH)₂ + SO₂).
- 1 — Correct balanced equation for Strategy B (CaCO₃ or Ca(OH)₂ with H⁺ in lake).
- 1 — Compares strategies on scope (source vs consequence), explaining chemistry.
- 1 — Compares strategies on permanence / ongoing vs one-off, with reasoning.
- 1 — Compares strategies on one further criterion (by-products, cost, speed, scale).
- 1 — Justifies a combination approach linking it explicitly to both the lake and the ongoing SO₂ issue.
- 1 — Identifies one limitation that neither strategy addresses (CO₂ / climate / ocean acidification, or equivalent valid limitation).