Level 2 — RecallChemical Kinetics

Chemical Kinetics

30 minutes40 marksprintable — key stays hidden on paper

Level: 2 (Recall — definitions, standard problems, short derivations) Time Limit: 30 minutes Total Marks: 40

Use R=8.314 J K1mol1R = 8.314\ \text{J K}^{-1}\text{mol}^{-1}, log\log values as needed. Show all working.


Q1. Define the following terms: (a) average rate of reaction, (b) instantaneous rate of reaction. State one method to obtain instantaneous rate graphically. (3 marks)

Q2. Distinguish between order and molecularity of a reaction, giving one point of difference and one example of each. (4 marks)

Q3. For a first-order reaction, starting from the differential rate law d[A]dt=k[A]-\dfrac{d[A]}{dt} = k[A], derive the integrated rate expression k=2.303tlog[A]0[A]k = \dfrac{2.303}{t}\log\dfrac{[A]_0}{[A]}. (4 marks)

Q4. Derive the expression for the half-life of a zero-order reaction and show that t1/2[A]0t_{1/2} \propto [A]_0. (4 marks)

Q5. A first-order reaction has a rate constant k=1.15×103 s1k = 1.15 \times 10^{-3}\ \text{s}^{-1}. Calculate the time required for the reactant to reduce to 14\tfrac{1}{4} of its initial concentration. (4 marks)

Q6. What is meant by a pseudo-first-order reaction? Explain with the example of acid hydrolysis of an ester, and state why it appears first order. (4 marks)

Q7. The rate constant of a reaction doubles when the temperature is raised from 300 K300\ \text{K} to 310 K310\ \text{K}. Calculate the activation energy EaE_a. (5 marks)

Q8. State the Arrhenius equation and explain each term. Sketch and label the Arrhenius plot (lnk\ln k vs 1/T1/T) and state how EaE_a is obtained from it. (4 marks)

Q9. Briefly explain the collision theory of reaction rates. Define the frequency factor and the steric (probability) factor. (4 marks)

Q10. Distinguish between homogeneous and heterogeneous catalysis with one example of each. State one characteristic of enzyme catalysis. (4 marks)


End of paper

Answer keyMark scheme & solutions

Q1. (3 marks)

  • (a) Average rate = change in concentration of reactant/product over a finite time interval: rateavg=Δ[A]Δt\text{rate}_{avg} = -\dfrac{\Delta[A]}{\Delta t}. (1)
  • (b) Instantaneous rate = rate at a particular instant, i.e. the limit as Δt0\Delta t \to 0: d[A]dt-\dfrac{d[A]}{dt}. (1)
  • Method: draw the tangent to the concentration–time curve at the given instant; its slope gives the instantaneous rate. (1)

Q2. (4 marks)

  • Order: sum of powers of concentration terms in the experimentally determined rate law; can be zero, fractional or integer; an experimental quantity. (1)
  • Molecularity: number of reacting species (atoms/molecules) colliding in an elementary step; always a whole number (1\geq 1); a theoretical quantity. (1)
  • Difference: order is experimental & may be fractional/zero, whereas molecularity is theoretical & always integral 1\geq 1. (1)
  • Examples: order — decomposition of N2O5N_2O_5 (first order); molecularity — 2HIH2+I22HI \to H_2 + I_2 (bimolecular). (1)

Q3. (4 marks) d[A]dt=k[A]    d[A][A]=kdt-\frac{d[A]}{dt} = k[A] \implies \frac{d[A]}{[A]} = -k\,dt (1) Integrate between limits [A]0[A]_0 (at t=0t=0) and [A][A] (at tt): [A]0[A]d[A][A]=k0tdt\int_{[A]_0}^{[A]}\frac{d[A]}{[A]} = -k\int_0^t dt (1) ln[A][A]0=kt    ln[A]0[A]=kt\ln\frac{[A]}{[A]_0} = -kt \implies \ln\frac{[A]_0}{[A]} = kt (1) Converting to base 10: k=2.303tlog[A]0[A]k = \dfrac{2.303}{t}\log\dfrac{[A]_0}{[A]}. (1)


Q4. (4 marks) Zero order: d[A]dt=k    d[A]=kdt-\dfrac{d[A]}{dt} = k \implies d[A] = -k\,dt. Integrating: [A]=[A]0kt[A] = [A]_0 - kt. (2) At half-life, [A]=[A]02[A] = \tfrac{[A]_0}{2}, t=t1/2t = t_{1/2}: [A]02=[A]0kt1/2    kt1/2=[A]02\frac{[A]_0}{2} = [A]_0 - k\,t_{1/2} \implies k\,t_{1/2} = \frac{[A]_0}{2} (1) t1/2=[A]02kt1/2[A]0\boxed{t_{1/2} = \frac{[A]_0}{2k}} \quad\Rightarrow\quad t_{1/2}\propto [A]_0 (1)


Q5. (4 marks) First order: t=2.303klog[A]0[A]t = \dfrac{2.303}{k}\log\dfrac{[A]_0}{[A]}. Here [A]=14[A]0[A] = \tfrac{1}{4}[A]_0, so ratio =4=4. (1) t=2.3031.15×103log4t = \frac{2.303}{1.15\times10^{-3}}\log 4 (1) log4=0.602\log 4 = 0.602; 2.3031.15×103=2002.6 s\dfrac{2.303}{1.15\times10^{-3}} = 2002.6\ \text{s}. (1) t=2002.6×0.6021.206×103 s1205 st = 2002.6 \times 0.602 \approx 1.206\times10^{3}\ \text{s} \approx 1205\ \text{s} (1)


Q6. (4 marks)

  • A pseudo-first-order reaction is one that is truly higher order but behaves as first order because one reactant is present in large excess (nearly constant). (1)
  • Example: CH3COOC2H5+H2OH+CH3COOH+C2H5OH\text{CH}_3\text{COOC}_2\text{H}_5 + H_2O \xrightarrow{H^+} \text{CH}_3\text{COOH} + C_2H_5OH. (1)
  • Rate =k[ester][H2O]= k[\text{ester}][H_2O]; water is in large excess so [H2O][H_2O] ≈ constant. (1)
  • Thus rate =k[ester]= k'[\text{ester}] where k=k[H2O]k' = k[H_2O]; the reaction appears first order. (1)

Q7. (5 marks) Arrhenius (two temperatures): logk2k1=Ea2.303R(1T11T2)\log\frac{k_2}{k_1} = \frac{E_a}{2.303R}\left(\frac{1}{T_1}-\frac{1}{T_2}\right) (1) k2/k1=2k_2/k_1 = 2, T1=300T_1=300, T2=310T_2=310. log2=0.301\log 2 = 0.301. (1) 13001310=310300300×310=1093000=1.0753×104\frac{1}{300}-\frac{1}{310} = \frac{310-300}{300\times310}=\frac{10}{93000}=1.0753\times10^{-4} (1) Ea=2.303×8.314×0.3011.0753×104E_a = \frac{2.303\times8.314\times0.301}{1.0753\times10^{-4}} (1) Ea=5.7631.0753×1045.36×104 J mol153.6 kJ mol1E_a = \frac{5.763}{1.0753\times10^{-4}} \approx 5.36\times10^{4}\ \text{J mol}^{-1} \approx 53.6\ \text{kJ mol}^{-1} (1)


Q8. (4 marks)

  • Arrhenius equation: k=AeEa/RTk = A\,e^{-E_a/RT}. (1)
  • AA = frequency/pre-exponential factor; EaE_a = activation energy; RR = gas constant; TT = absolute temperature; exponential term = fraction of effective collisions. (1)
  • Plot: lnk=lnAEaR1T\ln k = \ln A - \dfrac{E_a}{R}\cdot\dfrac{1}{T} — straight line, negative slope. (1)
  • Slope =Ea/REa=R×(slope)= -E_a/R \Rightarrow E_a = -R\times(\text{slope}); intercept =lnA= \ln A. (1)

Q9. (4 marks)

  • Collision theory: reactant molecules must collide for a reaction; rate depends on collision frequency and the fraction of collisions that are effective. (1)
  • Only collisions with energy Ea\geq E_a and proper orientation lead to product. (1)
  • Frequency factor (AA / ZZ): number of collisions per unit time per unit volume (collision frequency). (1)
  • Steric (probability) factor (PP): fraction of collisions with correct orientation; k=PZeEa/RTk = P\,Z\,e^{-E_a/RT}. (1)

Q10. (4 marks)

  • Homogeneous catalysis: catalyst and reactants in the same phase; e.g. 2SO2+O2NO2SO32SO_2 + O_2 \xrightarrow{NO} 2SO_3 (all gases) or acid-catalysed ester hydrolysis. (1.5)
  • Heterogeneous catalysis: catalyst in a different phase; e.g. Haber process N2+3H2Fe(s)2NH3N_2 + 3H_2 \xrightarrow{Fe(s)} 2NH_3. (1.5)
  • Enzyme catalysis: highly specific, efficient biological catalyst active under mild conditions (body temperature, near-neutral pH). (1)

[
  {"claim":"Q5: time for first-order reaction to reach 1/4 concentration ≈ 1205 s","code":"k=Rational(115,100000); t=(2.303/float(k))*float(log(4,10)); result = abs(t-1205)<10"},
  {"claim":"Q4: half-life of zero order = [A]0/(2k)","code":"A0,k,t=symbols('A0 k t',positive=True); sol=solve(Eq(A0-k*t, A0/2), t)[0]; result = simplify(sol - A0/(2*k))==0"},
  {"claim":"Q7: activation energy ≈ 53.6 kJ/mol","code":"Rg=8.314; Ea=(2.303*Rg*float(log(2,10)))/((1/300)-(1/310)); result = abs(Ea/1000-53.6)<1.0"},
  {"claim":"Q3: integrated first-order gives ln([A]0/[A])=kt","code":"A0,k,t,A=symbols('A0 k t A',positive=True); expr=solve(Eq(log(A/A0), -k*t), A)[0]; result = simplify(expr - A0*exp(-k*t))==0"}
]