Master all CBSE question paper patterns (As per Rationalised Syllabus). Includes extensive PYQs (2024, 2025, 2026): Rate Laws, Integrated Kinetics, Half-life, and Arrhenius Equation.
$$ -\frac{1}{2}\frac{d[N_2O_5]}{dt} = +\frac{1}{4}\frac{d[NO_2]}{dt} $$
$$ -\frac{d[N_2O_5]}{dt} = \frac{2}{4} \times \left(2.8 \times 10^{-3}\right) = \mathbf{1.4 \times 10^{-3} \text{ M s}^{-1}} $$
When the volume is reduced to half ($V' = V/2$), the concentration of all gases doubles since $C = n/V$.
New concentrations: $[A]' = 2[A]$, $[B]' = 2[B]$.
New rate $r_2 = k[A]'([B]')^2 = k(2[A])(2[B])^2 = 8k[A][B]^2 = 8 r_1$. The rate increases to 8 times.
Rate of reaction = $-\frac{1}{2}\frac{d[A]}{dt} = +\frac{d[P]}{dt}$
Given $-\frac{d[A]}{dt} = 0.05 \text{ M s}^{-1}$
Rate of reaction = $\frac{1}{2} \times 0.05 = \mathbf{0.025 \text{ M s}^{-1}}$
Rate of formation of P ($\frac{d[P]}{dt}$) = Rate of reaction = $\mathbf{0.025 \text{ M s}^{-1}}$
Rate = $-\frac{1}{4}\frac{d[NH_3]}{dt} = +\frac{1}{4}\frac{d[NO]}{dt} = +\frac{1}{6}\frac{d[H_2O]}{dt}$
Since the coefficients of $NH_3$ and $NO$ are both 4, rate of disappearance of $NH_3$ = rate of formation of $NO$ = $\mathbf{3.6 \times 10^{-3} \text{ M s}^{-1}}$.
For $H_2O$: $\frac{1}{6}\frac{d[H_2O]}{dt} = \frac{1}{4}\frac{d[NO]}{dt}$
$\frac{d[H_2O]}{dt} = \frac{6}{4} \times 3.6 \times 10^{-3} = 1.5 \times 3.6 \times 10^{-3} = \mathbf{5.4 \times 10^{-3} \text{ M s}^{-1}}$.
| Exp | [A] (mol/L) | [B] (mol/L) | Initial Rate (M/s) |
|---|---|---|---|
| 1 | 0.10 | 0.10 | $2.0 \times 10^{-3}$ |
| 2 | 0.10 | 0.20 | $4.0 \times 10^{-3}$ |
| 3 | 0.20 | 0.10 | $8.0 \times 10^{-3}$ |
Let the rate law be $\text{Rate} = k[A]^x[B]^y$.
From Exp 1 & 2: $[A]$ is constant. Doubling $[B]$ doubles the rate. $\Rightarrow \mathbf{y = 1}$
From Exp 1 & 3: $[B]$ is constant. Doubling $[A]$ quadruples the rate. $\Rightarrow \mathbf{x = 2}$
Rate Law: $\text{Rate} = k[A]^2[B]^1$
The unit of rate constant $k$ is: $(\text{mol L}^{-1})^{1-n} \text{ s}^{-1}$
(i) $\text{L mol}^{-1} \text{ s}^{-1} \Rightarrow 1 - n = -1 \Rightarrow \mathbf{n = 2}$ (Second Order)
(ii) $\text{s}^{-1} \Rightarrow 1 - n = 0 \Rightarrow \mathbf{n = 1}$ (First Order)
(iii) $\text{mol L}^{-1} \text{ s}^{-1} \Rightarrow 1 - n = 1 \Rightarrow \mathbf{n = 0}$ (Zero Order)
Overall order $n = 1 + \frac{1}{2} = \mathbf{\frac{3}{2}}$ or **1.5**.
Unit of $k = (\text{mol L}^{-1})^{1-n} \text{ s}^{-1}$
Unit $= (\text{mol L}^{-1})^{1 - 1.5} \text{ s}^{-1} = (\text{mol L}^{-1})^{-0.5} \text{ s}^{-1}$
Unit = $\mathbf{\text{L}^{1/2} \text{mol}^{-1/2} \text{ s}^{-1}}$
Rate law: $\text{Rate} = k[A]^0[B]^2 = k[B]^2$
If concentrations of both A and B are doubled, $[A] \rightarrow 2[A]$ and $[B] \rightarrow 2[B]$.
New Rate = $k(2[B])^2 = 4k[B]^2$.
The rate increases to **4 times** its original value. (Changes in A have no effect because it is zero order w.r.t A).
For a first order reaction: $t = \frac{2.303}{k} \log \frac{[R]_0}{[R]}$
Given: $k = 60 \text{ s}^{-1}$, $[R] = \frac{[R]_0}{16}$.
$$ t = \frac{2.303}{60} \log (16) = \frac{2.303 \times 1.204}{60} = \mathbf{4.62 \times 10^{-2} \text{ s}} $$
For 99.9% completion: $[R] = 0.1\%$ of $[R]_0$
$$ t_{99.9\%} = \frac{2.303}{k} \log \frac{100}{0.1} = \frac{2.303}{k} \log 1000 = \frac{6.909}{k} $$
$$ t_{1/2} = \frac{0.693}{k} $$
$$ \frac{t_{99.9\%}}{t_{1/2}} = \frac{6.909}{0.693} \approx 10 \Rightarrow \mathbf{t_{99.9\%} = 10 \times t_{1/2}} $$
For 99% completion: $[R] = 1\%$ of $[R]_0 = 1$ (if $[R]_0 = 100$).
$$ t_{99\%} = \frac{2.303}{k} \log \frac{100}{1} = \frac{2.303}{k} \log 100 = \frac{2.303 \times 2}{k} = \frac{4.606}{k} $$
For 90% completion: $[R] = 10\%$ of $[R]_0 = 10$.
$$ t_{90\%} = \frac{2.303}{k} \log \frac{100}{10} = \frac{2.303}{k} \log 10 = \frac{2.303 \times 1}{k} $$
Comparing the two: $\mathbf{t_{99\%} = 2 \times t_{90\%}}$ (Hence Proved).
Case 1 (25% decomp): $[R] = 75$, $t = 20 \text{ min}$
$$ k = \frac{2.303}{20} \log \frac{100}{75} = \frac{2.303}{20} \log \frac{4}{3} = \frac{2.303}{20} (0.6021 - 0.4771) = \frac{2.303 \times 0.125}{20} $$
$$ k = 0.01439 \text{ min}^{-1} $$
Case 2 (75% decomp): $[R] = 25$
$$ t = \frac{2.303}{k} \log \frac{100}{25} = \frac{2.303}{0.01439} \log 4 = 160.04 \times 0.6021 = \mathbf{96.36 \text{ min}} $$
For a zero-order reaction: $k = \frac{[R]_0 - [R]}{t}$. Slope of $[R]$ vs $t$ is **$-k$**.
Case 1 (20% complete): $k = \frac{100 - 80}{10} = 2 \text{ mol L}^{-1}\text{min}^{-1}$
Case 2 (80% complete): $2 = \frac{100 - 20}{t} \Rightarrow t = \frac{80}{2} = \mathbf{40 \text{ minutes}}$
$$ k = \frac{0.693}{5730} \text{ yr}^{-1} $$
$$ t = \frac{2.303}{k} \log \frac{100}{80} = \frac{2.303 \times 5730}{0.693} \log 1.25 $$
$$ t = 19041.8 \times 0.0969 = \mathbf{1845 \text{ years}} $$
For a zero order reaction, the half-life is given by:
$$ t_{1/2} = \frac{[R]_0}{2k} $$
Given $[R]_0 = 0.1 \text{ M}$ and $k = 0.003 \text{ M s}^{-1}$.
$$ t_{1/2} = \frac{0.1}{2 \times 0.003} = \frac{0.1}{0.006} = \mathbf{16.67 \text{ s}} $$
For a zero order reaction, $\text{Rate} = k[NH_3]^0 = k = 2.5 \times 10^{-4} \text{ mol L}^{-1} \text{ s}^{-1}$.
From stoichiometry: Rate = $-\frac{1}{2}\frac{d[NH_3]}{dt} = \frac{d[N_2]}{dt} = \frac{1}{3}\frac{d[H_2]}{dt}$
Rate of production of $N_2$ ($\frac{d[N_2]}{dt}$) = Rate = $\mathbf{2.5 \times 10^{-4} \text{ mol L}^{-1} \text{ s}^{-1}}$.
Rate of production of $H_2$ ($\frac{d[H_2]}{dt}$) = $3 \times \text{Rate} = 3 \times (2.5 \times 10^{-4}) = \mathbf{7.5 \times 10^{-4} \text{ mol L}^{-1} \text{ s}^{-1}}$.
Given: $T_1 = 300\text{K}$, $T_2 = 301\text{K}$, $\frac{k_2}{k_1} = 1.05$.
$$ \log(1.05) = \frac{E_a}{2.303 \times 8.314} \left[ \frac{301 - 300}{300 \times 301} \right] $$
$$ 0.0212 = \frac{E_a}{19.147} \left[ \frac{1}{90300} \right] \Rightarrow \mathbf{E_a = 36.65 \text{ kJ mol}^{-1}} $$
Fraction of molecules $x = e^{-E_a / RT}$. Taking log: $\log x = -\frac{E_a}{2.303 RT}$
$$ \log x = -\frac{209500}{2.303 \times 8.314 \times 581} = -18.832 $$
$$ x = \text{Antilog} (-18.832) = \mathbf{1.47 \times 10^{-19}} $$
According to Arrhenius Equation: $\log k = \log A - \frac{E_a}{2.303 RT}$
$$ \log(1.5 \times 10^{-4}) = \log A - \frac{50000}{2.303 \times 8.314 \times 300} $$
$$ \log 1.5 - 4 = \log A - 8.71 $$
$$ 0.176 - 4 = \log A - 8.71 \Rightarrow -3.824 = \log A - 8.71 $$
$$ \log A = 8.71 - 3.824 = 4.886 $$
$$ A = \text{Antilog}(4.886) = \mathbf{7.69 \times 10^4 \text{ s}^{-1}} $$
Given: $T_1 = 20^\circ\text{C} = 293\text{K}$, $T_2 = 50^\circ\text{C} = 323\text{K}$, $\frac{k_2}{k_1} = 3$.
$$ \log \frac{k_2}{k_1} = \frac{E_a}{2.303 R} \left[ \frac{T_2 - T_1}{T_1 T_2} \right] $$
$$ \log 3 = \frac{E_a}{2.303 \times 8.314} \left[ \frac{323 - 293}{293 \times 323} \right] $$
$$ 0.4771 = \frac{E_a}{19.147} \left[ \frac{30}{94639} \right] $$
$$ E_a = \frac{0.4771 \times 19.147 \times 94639}{30} = 28815 \text{ J mol}^{-1} $$
$$ \mathbf{E_a = 28.81 \text{ kJ mol}^{-1}} $$
Reaction: $\text{CH}_3\text{COOC}_2\text{H}_5 + \text{H}_2\text{O} \xrightarrow{\text{H}^+} \text{CH}_3\text{COOH} + \text{C}_2\text{H}_5\text{OH}$
Because water is present in such a large excess, its concentration remains almost constant. Therefore, the term $k'[\text{H}_2\text{O}]$ is taken as a new constant $k$.
New Rate Law: $\text{Rate} = k[\text{CH}_3\text{COOC}_2\text{H}_5]$, behaving as first-order.
At time $t$, $P_A = 2P_i - P_t$
At $t = 100 \text{ s}$, $P_t = 0.6 \text{ atm}$. $P_A = 2(0.5) - 0.6 = 0.4 \text{ atm}$
$$ k = \frac{2.303}{100} \log \frac{0.5}{0.4} = \frac{2.303}{100} \log(1.25) = \frac{2.303 \times 0.0969}{100} = \mathbf{2.23 \times 10^{-3} \text{ s}^{-1}} $$
Reaction: $\text{C}_{12}\text{H}_{22}\text{O}_{11} + \text{H}_2\text{O} \xrightarrow{\text{H}^+} \text{C}_6\text{H}_{12}\text{O}_6 (\text{glucose}) + \text{C}_6\text{H}_{12}\text{O}_6 (\text{fructose})$
Rate Law: $\text{Rate} = k[\text{C}_{12}\text{H}_{22}\text{O}_{11}]$
It is pseudo-first order because although both cane sugar and water are reactants (making it theoretically a second-order reaction), water is present in huge excess. Its concentration does not change significantly during the reaction, making the rate dependent only on the concentration of cane sugar.
Given 50% decomposition is $t_{1/2} = 120 \text{ min}$.
$$ k = \frac{0.693}{120} = 0.005775 \text{ min}^{-1} $$
For 90% decomposition: $[R] = 100 - 90 = 10$
$$ t_{90\%} = \frac{2.303}{k} \log \frac{100}{10} = \frac{2.303}{0.005775} \log(10) $$
$$ t_{90\%} = \frac{2.303}{0.005775} = \mathbf{398.8 \text{ min}} $$