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This lesson brings together kinetics and equilibrium in the kind of multi-step problems that appear in Edexcel A-level exams. We will work through extended calculations combining rate equations, the Arrhenius equation, ICE tables, and Kp calculations, building the fluency you need for the exam.
The reaction X + 2Y → Z was studied using the initial rate method:
| Experiment | [X] / mol dm⁻³ | [Y] / mol dm⁻³ | Initial rate / mol dm⁻³ s⁻¹ |
|---|---|---|---|
| 1 | 0.10 | 0.10 | 3.2 × 10⁻³ |
| 2 | 0.10 | 0.20 | 1.28 × 10⁻² |
| 3 | 0.20 | 0.10 | 6.4 × 10⁻³ |
Step 1: Determine order with respect to Y.
Compare Experiments 1 and 2 ([X] constant):
[Y] doubles (0.10 → 0.20). Rate changes: 1.28 × 10⁻² / 3.2 × 10⁻³ = 4.0 = 2²
Order with respect to Y = 2
Step 2: Determine order with respect to X.
Compare Experiments 1 and 3 ([Y] constant):
[X] doubles (0.10 → 0.20). Rate changes: 6.4 × 10⁻³ / 3.2 × 10⁻³ = 2.0 = 2¹
Order with respect to X = 1
Step 3: Write the rate equation.
Rate = k[X][Y]² (overall order = 3)
Step 4: Calculate k using data from any experiment (use Experiment 1).
k = Rate / ([X][Y]²) = 3.2 × 10⁻³ / (0.10 × (0.10)²) = 3.2 × 10⁻³ / 1.0 × 10⁻³ = 3.2 mol⁻² dm⁶ s⁻¹
Step 5: Verify k with another experiment (Experiment 2).
k = 1.28 × 10⁻² / (0.10 × (0.20)²) = 1.28 × 10⁻² / (0.10 × 0.04) = 1.28 × 10⁻² / 4.0 × 10⁻³ = 3.2 mol⁻² dm⁶ s⁻¹ ✓
Step 6: Predict the rate for [X] = 0.30, [Y] = 0.15.
Rate = 3.2 × (0.30) × (0.15)² = 3.2 × 0.30 × 0.0225 = 0.0216 mol dm⁻³ s⁻¹
The reaction 2A + B → C + D has the rate equation Rate = k[A][B].
The overall order is 2, and both A and B appear in the rate equation with order 1 each.
What does this tell us about the mechanism?
Since the rate equation is first order in A (not second order as the stoichiometric coefficient might suggest), the rate-determining step involves one molecule of A and one molecule of B:
Slow step (RDS): A + B → intermediate
Fast step: intermediate + A → C + D
This mechanism is consistent with the rate equation because only species in or before the RDS appear in the rate equation.
For a first-order reaction, k₁ = 2.5 × 10⁻³ s⁻¹ at 290 K and k₂ = 1.0 × 10⁻² s⁻¹ at 310 K.
Step 1: Use the two-temperature form.
ln(k₂/k₁) = (Ea/R)(1/T₁ − 1/T₂)
ln(1.0 × 10⁻² / 2.5 × 10⁻³) = (Ea/8.314)(1/290 − 1/310)
Step 2: Calculate each side.
ln(4.0) = 1.386
1/290 − 1/310 = (310 − 290)/(290 × 310) = 20/89900 = 2.225 × 10⁻⁴ K⁻¹
Step 3: Solve for Ea.
Ea = 1.386 × 8.314 / 2.225 × 10⁻⁴ = 11.52 / 2.225 × 10⁻⁴ = 51 800 J mol⁻¹ = 51.8 kJ mol⁻¹
Using the Ea calculated above (51.8 kJ mol⁻¹), predict k at 330 K.
ln(k₃/k₁) = (Ea/R)(1/T₁ − 1/T₃)
ln(k₃/2.5 × 10⁻³) = (51800/8.314)(1/290 − 1/330)
1/290 − 1/330 = (330 − 290)/(290 × 330) = 40/95700 = 4.179 × 10⁻⁴ K⁻¹
ln(k₃/2.5 × 10⁻³) = 6230 × 4.179 × 10⁻⁴ = 2.604
k₃/2.5 × 10⁻³ = e^2.604 = 13.52
k₃ = 13.52 × 2.5 × 10⁻³ = 0.0338 s⁻¹
A first-order reaction has t½ = 100 s at 300 K and t½ = 25 s at 320 K.
Step 1: Calculate k at each temperature.
k₁ = ln 2 / t½ = 0.693 / 100 = 0.00693 s⁻¹ (at 300 K) k₂ = ln 2 / 25 = 0.0277 s⁻¹ (at 320 K)
Step 2: Use the Arrhenius two-temperature form.
ln(k₂/k₁) = (Ea/R)(1/T₁ − 1/T₂)
ln(0.0277/0.00693) = (Ea/8.314)(1/300 − 1/320)
ln(4.0) = (Ea/8.314)(2.083 × 10⁻⁴)
1.386 = (Ea/8.314)(2.083 × 10⁻⁴)
Ea = 1.386 × 8.314 / 2.083 × 10⁻⁴ = 55 300 J mol⁻¹ = 55.3 kJ mol⁻¹
0.200 mol of A and 0.200 mol of B are placed in a 1.00 dm³ flask. At equilibrium, Kc = 4.00 for A(g) + B(g) ⇌ C(g) + D(g). Find [C] at equilibrium.
| A | B | C | D | |
|---|---|---|---|---|
| Initial | 0.200 | 0.200 | 0 | 0 |
| Change | −x | −x | +x | +x |
| Equilibrium | 0.200−x | 0.200−x | x | x |
Kc = [C][D] / ([A][B]) = x² / (0.200 − x)² = 4.00
Taking the square root: x / (0.200 − x) = 2.00
x = 2.00(0.200 − x) = 0.400 − 2.00x
3.00x = 0.400
x = 0.133 mol dm⁻³
[C] = 0.133 mol dm⁻³ (and [A] = [B] = 0.200 − 0.133 = 0.067 mol dm⁻³)
Check: Kc = (0.133)² / (0.067)² = 0.01769 / 0.004489 = 3.94 ≈ 4.00 ✓ (rounding)
0.300 mol of A and 0.100 mol of B in a 1.00 dm³ flask. Kc = 10.0 for A + B ⇌ C.
| A | B | C | |
|---|---|---|---|
| Initial | 0.300 | 0.100 | 0 |
| Change | −x | −x | +x |
| Equilibrium | 0.300 − x | 0.100 − x | x |
Kc = x / ((0.300 − x)(0.100 − x)) = 10.0
x = 10.0 × (0.0300 − 0.300x − 0.100x + x²)
x = 10.0 × (0.0300 − 0.400x + x²)
x = 0.300 − 4.00x + 10.0x²
10.0x² − 5.00x + 0.300 = 0
Using the quadratic formula: x = (5.00 ± √(25.00 − 12.00)) / 20.0 = (5.00 ± √13.00) / 20.0
x = (5.00 ± 3.606) / 20.0
x = 8.606/20.0 = 0.430 (rejected -- exceeds [B]₀ = 0.100)
x = 1.394/20.0 = 0.0697 mol dm⁻³
Check: Kc = 0.0697 / ((0.300 − 0.0697)(0.100 − 0.0697)) = 0.0697 / (0.2303 × 0.0303) = 0.0697 / 0.00698 = 9.99 ≈ 10.0 ✓
Key insight: Always check both roots of the quadratic. Reject any root that gives a negative concentration.
2.00 mol of SO₃ is placed in a container and heated to 1000 K at a total pressure of 1.50 atm. At equilibrium, 40.0% of SO₃ has dissociated:
2SO₃(g) ⇌ 2SO₂(g) + O₂(g)
Step 1: ICE table in moles.
40% of 2.00 = 0.80 mol SO₃ dissociates.
| 2SO₃ | 2SO₂ | O₂ | |
|---|---|---|---|
| Initial | 2.00 | 0 | 0 |
| Change | −0.80 | +0.80 | +0.40 |
| Equilibrium | 1.20 | 0.80 | 0.40 |
(Ratio: 2:2:1, so 0.80 mol SO₂ and 0.40 mol O₂ formed)
Step 2: Total moles and mole fractions.
Total = 1.20 + 0.80 + 0.40 = 2.40 mol
x(SO₃) = 1.20/2.40 = 0.500 x(SO₂) = 0.80/2.40 = 0.333 x(O₂) = 0.40/2.40 = 0.167
Check: 0.500 + 0.333 + 0.167 = 1.000 ✓
Step 3: Partial pressures.
p(SO₃) = 0.500 × 1.50 = 0.750 atm p(SO₂) = 0.333 × 1.50 = 0.500 atm p(O₂) = 0.167 × 1.50 = 0.250 atm
Check: 0.750 + 0.500 + 0.250 = 1.500 atm ✓
Step 4: Calculate Kp.
Kp = p(SO₂)² × p(O₂) / p(SO₃)²
Kp = (0.500)² × 0.250 / (0.750)²
Kp = 0.250 × 0.250 / 0.5625
Kp = 0.0625 / 0.5625
Kp = 0.111 atm
Units: atm² × atm / atm² = atm ✓
For the equilibrium: A + B ⇌ C
The forward rate equation is: Rate_forward = k_f[A][B]
The reverse rate equation is: Rate_reverse = k_r[C]
At equilibrium, Rate_forward = Rate_reverse:
k_f[A][B] = k_r[C]
Rearranging: [C] / ([A][B]) = k_f / k_r = Kc
This shows that Kc = k_f / k_r -- the equilibrium constant equals the ratio of the forward and reverse rate constants. This is a fundamental link between kinetics and equilibrium.
Worked Example: At 500 K, k_f = 0.040 mol⁻¹ dm³ s⁻¹ and k_r = 0.0080 s⁻¹.
Kc = k_f / k_r = 0.040 / 0.0080 = 5.0 mol⁻¹ dm³
Implication: If temperature increases and Ea(forward) < Ea(reverse), then k_f increases more slowly than k_r, so Kc decreases. This is consistent with the exothermic forward reaction being disfavoured by higher temperature.
For A ⇌ B with ΔH = −30 kJ mol⁻¹ (exothermic forward):
At 300 K: k_f = 0.050 s⁻¹, k_r = 0.010 s⁻¹. Kc = 0.050/0.010 = 5.0
The forward reaction has Ea(f) = 60 kJ mol⁻¹. Since ΔH = Ea(f) − Ea(r), we get Ea(r) = 60 + 30 = 90 kJ mol⁻¹.
At 350 K, both k values increase, but k_r increases more (it has higher Ea):
Using Arrhenius for k_f: ln(k_f'/0.050) = (60000/8.314)(1/300 − 1/350) = 7216 × 4.762 × 10⁻⁴ = 3.437
k_f' = 0.050 × e^3.437 = 0.050 × 31.1 = 1.55 s⁻¹
Using Arrhenius for k_r: ln(k_r'/0.010) = (90000/8.314)(1/300 − 1/350) = 10824 × 4.762 × 10⁻⁴ = 5.154
k_r' = 0.010 × e^5.154 = 0.010 × 173.2 = 1.73 s⁻¹
New Kc = 1.55/1.73 = 0.90
Kc has decreased from 5.0 to 0.90 -- consistent with Le Chatelier's prediction that increasing temperature shifts an exothermic equilibrium to the left.
| Problem type | Key steps | Common error to avoid |
|---|---|---|
| Rate equation from data | Compare pairs with one variable constant | Comparing experiments where both concentrations change |
| Calculate k | k = Rate / [A]^m[B]^n; verify with all experiments | Wrong units for k |
| Arrhenius (two temps) | Use ln(k₂/k₁) = (Ea/R)(1/T₁ − 1/T₂) | Ea in kJ instead of J; T in °C instead of K |
| ICE table for Kc | Moles → concentrations; check stoichiometry | Forgetting to divide by volume |
| Kp calculation | Moles → mole fractions → partial pressures → Kp | Mole fractions not summing to 1 |
| Quadratic ICE | Use quadratic formula; reject unphysical root | Accepting a root that gives negative concentration |
| Kc from rate constants | Kc = k_f / k_r | Inverting the ratio |
This lesson has demonstrated how to combine rate equations, Arrhenius calculations, ICE tables, and Kp calculations in extended problems. The link Kc = k_f/k_r connects kinetics and equilibrium quantitatively. Practice these problem types until the procedures become fluent -- they are heavily examined.
Edexcel 9CH0 specification, Topics 9, 10, 11 and 16 combined — synoptic kinetics and equilibrium problem solving requires candidates to integrate rate-determination methods (Topic 9), order analysis and Arrhenius (Topic 16), Le Chatelier (Topic 10) and equilibrium constants Kc/Kp (Topics 10 and 11) into multi-part questions that may also draw on Topic 8 (energetics), Topic 17 (organic mechanisms — SN1/SN2), Topic 19 (transition metal catalysis) and CP5/CP8/CP11 (refer to the official specification document for exact wording). Synoptic kinetics-and-equilibrium questions are examined principally on Paper 3 (synoptic, ~30% of the A-Level), where candidates are expected to draw connections across the whole specification, often within a single 12+ mark question. The data booklet provides Arrhenius, R and selected thermodynamic data; rate equations, K expressions, Le Chatelier shifts must be derived/applied from first principles.
Question (12 marks — synoptic):
The reaction H2(g)+I2(g)⇌2HI(g) is studied. Initial-rate data at 700 K:
| Exp | [H₂]₀ / mol dm⁻³ | [I₂]₀ / mol dm⁻³ | Initial rate / mol dm⁻³ s⁻¹ |
|---|---|---|---|
| 1 | 0.010 | 0.010 | 1.20 × 10⁻⁵ |
| 2 | 0.020 | 0.010 | 2.40 × 10⁻⁵ |
| 3 | 0.020 | 0.030 | 7.20 × 10⁻⁵ |
At 700 K, equilibrium analysis gives [H₂] = 0.020, [I₂] = 0.020, [HI] = 0.140 mol dm⁻³. Kc at 800 K is 50.7. ΔH=−10 kJ mol⁻¹.
(a) Determine orders, rate equation and k at 700 K. (4)
(b) Calculate Kc at 700 K. (2)
(c) Compare Kc at 700 K and 800 K and explain qualitatively. (2)
(d) Calculate Ea given k(700)=0.120 mol⁻¹ dm³ s⁻¹ (from your part (a)) and k(800)=0.580 mol⁻¹ dm³ s⁻¹. (3)
(e) Predict the effect of doubling total pressure on (i) rate; (ii) equilibrium position. (1)
Solution with mark scheme:
(a) M1 — Exp 1 vs 2: [H₂] doubles, rate doubles → 1st order in H₂. Exp 2 vs 3: [I₂] triples, rate triples → 1st order in I₂. A1 — overall 2nd order; rate = k[H2][I2]. M1 — substitute Exp 1: 1.20×10−5=k×0.010×0.010, k=0.120 mol⁻¹ dm³ s⁻¹. A1 — units derived from algebra.
(b) M1 — Kc=[HI]2/([H2][I2])=(0.140)2/(0.020×0.020)=0.0196/0.000400. A1 — Kc(700)=49.0, dimensionless (Δn=0).
(c) M1 — Kc(800) = 50.7 > Kc(700) = 49.0; Kc increased slightly with T. A1 — but the reaction is exothermic (ΔH=−10 kJ mol⁻¹), so Le Chatelier predicts Kc should decrease with increased T. The fact that Kc barely changes (and even rises slightly) reflects the small ∣ΔH∣: the van't Hoff equation gives ΔlnK=−ΔH/R⋅(1/T2−1/T1) — for small ΔH, the change is small. The slight rise may indicate experimental scatter; sign-prediction from Le Chatelier is rigorously correct only if ΔH is significantly negative.
(d) M1 — Arrhenius two-point: ln(k2/k1)=(Ea/R)(1/T1−1/T2). M1 — ln(0.580/0.120)=ln(4.83)=1.575. 1/T1−1/T2=1/700−1/800=1.429×10−3−1.250×10−3=1.79×10−4 K⁻¹. A1 — Ea=R×1.575/1.79×10−4=8.31×8800=73×103 J mol⁻¹ = 73 kJ mol⁻¹.
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