Chemical Kinetics Formula Sheet
All key Chemical Kinetics formulas: rate laws, integrated rate equations, half-life, Arrhenius equation, and catalysis. JEE Main & Advanced quick revision.
Last-minute revision sheet for the entire Chemical Kinetics chapter: rate of reaction, rate law, order and molecularity, integrated rate equations, half-life, the Arrhenius equation, and catalysis. Every formula, relation, and shortcut below is pulled straight from the chapter pages.
Chapter Map
graph TD
A[Chemical Kinetics] --> B[Rate of Reaction]
A --> C[Rate Law & Order]
A --> D[Integrated Rate Laws]
A --> E[Half-Life]
A --> F[Arrhenius / Temperature]
A --> G[Catalysis]
C --> C1[Order vs Molecularity]
C --> C2[Units of k]
D --> D1[Zero / First / Second]
F --> F1[Activation Energy]
F --> F2[Collision Theory]Rate of Reaction
For a general reaction $aA + bB \rightarrow cC + dD$, the unique rate (divide by stoichiometric coefficients):
$$\boxed{r = -\frac{1}{a}\frac{d[A]}{dt} = -\frac{1}{b}\frac{d[B]}{dt} = +\frac{1}{c}\frac{d[C]}{dt} = +\frac{1}{d}\frac{d[D]}{dt}}$$| Quantity | Formula | Notes |
|---|---|---|
| Average rate | $r_{avg} = -\dfrac{\Delta[R]}{\Delta t} = +\dfrac{\Delta[P]}{\Delta t}$ | Over finite interval (slope of chord) |
| Instantaneous rate | $r = -\dfrac{d[R]}{dt} = +\dfrac{d[P]}{dt}$ | At one instant (slope of tangent) |
| Units of rate | $\text{mol L}^{-1}\text{s}^{-1}$ or $\text{M s}^{-1}$ | Always positive when called “rate of reaction” |
Rate Law and Rate Constant
For $aA + bB \rightarrow \text{Products}$:
$$\boxed{r = k[A]^m[B]^n}$$- $k$ = rate constant (specific rate constant)
- $m$ = order w.r.t. A, $n$ = order w.r.t. B
- Overall order $= m + n$ ( determined experimentally, not from stoichiometry)
Units of Rate Constant
$$\boxed{\text{Units of } k = (\text{concentration})^{1-n} \times (\text{time})^{-1}}$$| Order $n$ | Rate law | Units of $k$ |
|---|---|---|
| 0 | $r = k$ | mol L⁻¹ s⁻¹ (M s⁻¹) |
| 1 | $r = k[A]$ | s⁻¹ |
| 2 | $r = k[A]^2$ or $k[A][B]$ | L mol⁻¹ s⁻¹ (M⁻¹ s⁻¹) |
| 3 | $r = k[A]^2[B]$ | L² mol⁻² s⁻¹ (M⁻² s⁻¹) |
| $n$ | — | L⁽ⁿ⁻¹⁾ mol⁽¹⁻ⁿ⁾ s⁻¹ |
Initial Rate Method
Comparing two experiments where only one concentration changes:
$$\frac{r_2}{r_1} = \left(\frac{[A]_2}{[A]_1}\right)^{m} \implies 2^m = \frac{r_2}{r_1}\ \text{(if conc. doubled)}$$Order vs Molecularity
| Property | Order | Molecularity |
|---|---|---|
| Definition | Sum of powers in rate law | No. of molecules colliding in elementary step |
| Determination | Experimental | From mechanism (theoretical) |
| Value | 0, fractional, integer, negative | Only positive integer (1, 2, 3) |
| Can be zero / fraction? | Yes | No |
| Max value | No limit | 3 (termolecular, rare) |
| Applies to | Overall or elementary | Elementary steps only |
- For an elementary reaction: order = molecularity, and the rate law follows directly from stoichiometry.
- For a complex reaction: the rate-determining (slowest) step sets the rate law, so order may differ from stoichiometry (e.g. $2N_2O_5 \rightarrow 4NO_2 + O_2$ is first order, $r = k[N_2O_5]$).
- Fractional order examples: $CH_3CHO \rightarrow CH_4 + CO$ is order 1.5; $CHCl_3 + Cl_2$ is order 1.5.
Pseudo-First-Order Reactions
When one reactant is in large excess its concentration stays nearly constant:
$$r = k[A][B] \approx k'[A], \quad \text{where } k' = k[B]$$Example — acid hydrolysis of ester (water in excess):
$$CH_3COOC_2H_5 + H_2O \xrightarrow{H^+} CH_3COOH + C_2H_5OH$$Integrated Rate Equations
Zero Order
$$-\frac{d[A]}{dt} = k \qquad \boxed{[A]_t = [A]_0 - kt}$$First Order
$$-\frac{d[A]}{dt} = k[A]$$$$\boxed{\ln\frac{[A]_0}{[A]_t} = kt} \qquad k = \frac{2.303}{t}\log\frac{[A]_0}{[A]_t}$$$$[A]_t = [A]_0\, e^{-kt}$$Second Order (Type I: $r = k[A]^2$)
$$-\frac{d[A]}{dt} = k[A]^2 \qquad \boxed{\frac{1}{[A]_t} = \frac{1}{[A]_0} + kt}$$Type II ($r = k[A][B]$, with $[A]_0 \neq [B]_0$):
$$\frac{1}{[A]_0 - [B]_0}\ln\frac{[B]_0[A]_t}{[A]_0[B]_t} = kt$$Master Summary Table
| Order | Differential | Integrated | Linear plot | Slope | Half-life | $k$ units |
|---|---|---|---|---|---|---|
| 0 | $-\frac{d[A]}{dt}=k$ | $[A]_t=[A]_0-kt$ | $[A]$ vs $t$ | $-k$ | $\frac{[A]_0}{2k}$ | M s⁻¹ |
| 1 | $-\frac{d[A]}{dt}=k[A]$ | $\ln[A]_t=\ln[A]_0-kt$ | $\ln[A]$ vs $t$ | $-k$ | $\frac{0.693}{k}$ | s⁻¹ |
| 2 | $-\frac{d[A]}{dt}=k[A]^2$ | $\frac{1}{[A]_t}=\frac{1}{[A]_0}+kt$ | $\frac{1}{[A]}$ vs $t$ | $+k$ | $\frac{1}{k[A]_0}$ | M⁻¹ s⁻¹ |
First-Order Completion Shortcuts
$$t_{90\%} = \frac{2.303}{k}, \qquad t_{99\%} = \frac{2\times 2.303}{k} = 2\,t_{90\%}$$So $t_{99\%} = 2\,t_{90\%}$ for any first-order reaction.
Half-Life
$$\text{Half-life } t_{1/2}: \text{ time for } [A]_t = \frac{[A]_0}{2}$$After $n$ half-lives:
$$\boxed{\frac{[A]_t}{[A]_0} = \left(\frac{1}{2}\right)^{n}}$$| Order | $t_{1/2}$ | Dependence on $[A]_0$ | Successive half-lives |
|---|---|---|---|
| 0 | $\dfrac{[A]_0}{2k}$ | $\propto [A]_0$ | Decrease (1, ½, ¼, …) |
| 1 | $\dfrac{0.693}{k} = \dfrac{\ln 2}{k}$ | Independent | Constant (1, 1, 1, …) |
| 2 | $\dfrac{1}{k[A]_0}$ | $\propto \dfrac{1}{[A]_0}$ | Increase (1, 2, 4, …) |
Mean (Average) Life — First Order
$$\boxed{\tau = \frac{1}{k} = 1.443\, t_{1/2}}, \qquad t_{1/2} = 0.693\,\tau$$Order from Half-Life
$$\frac{t_{1/2}^{(1)}}{t_{1/2}^{(2)}} = \left(\frac{[A]_0^{(1)}}{[A]_0^{(2)}}\right)^{1-n}$$Arrhenius Equation and Activation Energy
$$\boxed{k = A\,e^{-E_a/RT}}$$- $A$ = pre-exponential / frequency factor
- $E_a$ = activation energy, $R = 8.314\ \text{J mol}^{-1}\text{K}^{-1}$, $T$ in Kelvin
Logarithmic Forms ($\ln k$ vs $1/T$ is a straight line)
$$\ln k = \ln A - \frac{E_a}{RT} \qquad \log k = \log A - \frac{E_a}{2.303RT}$$Slope of $\ln k$ vs $1/T$ plot $= -\dfrac{E_a}{R}$, intercept $= \ln A$, so $E_a = -\text{slope}\times R$.
Two-Temperature Form (most used in JEE)
$$\boxed{\ln\frac{k_2}{k_1} = \frac{E_a}{R}\left(\frac{1}{T_1} - \frac{1}{T_2}\right)}$$$$\log\frac{k_2}{k_1} = \frac{E_a}{2.303R}\left(\frac{1}{T_1} - \frac{1}{T_2}\right)$$Energy Profile Relations
$$\boxed{\Delta H = E_{a,\text{forward}} - E_{a,\text{reverse}}}$$- Exothermic ($\Delta H < 0$): $E_{a,f} < E_{a,r}$
- Endothermic ($\Delta H > 0$): $E_{a,f} > E_{a,r}$
Temperature Coefficient
$$Q_{10} = \frac{k_{T+10}}{k_T} \approx 2\ \text{to}\ 3 \quad (\text{rate roughly doubles per } 10^\circ\text{C rise})$$Catalyst Rate Enhancement
$$\boxed{\frac{k_{cat}}{k_{uncat}} = e^{-(E_{a,cat} - E_{a,uncat})/RT}}$$graph LR
A[Reactants] -->|"Ea forward"| B[Activated Complex]
B -->|"Ea reverse"| C[Products]- Always use Kelvin, never Celsius, in the exponential term.
- Match units: if $E_a$ is in kJ/mol use $R = 8.314\times10^{-3}$ kJ mol⁻¹ K⁻¹.
- Slope of $\ln k$ vs $1/T$ is negative ($-E_a/R$); $E_a$ itself is always positive.
- $\Delta H \neq E_a$. They are different quantities.
Collision Theory
$$r = Z \times f \times p, \qquad f = e^{-E_a/RT}$$$$k = Z\,p\,e^{-E_a/RT} \implies A = Z \times p$$- $Z$ = collision frequency
- $f$ = fraction of molecules with energy $\geq E_a$
- $p$ = steric (orientation) factor
A reaction occurs only when molecules collide, with energy $\geq E_a$, and proper orientation.
Catalysis
A catalyst provides an alternative pathway with lower $E_a$, so $k_{cat} \gg k_{uncat}$.
| Type | Phase relation | Key examples |
|---|---|---|
| Homogeneous | Catalyst same phase as reactants | $H^+$ in ester hydrolysis; NO in lead chamber process |
| Heterogeneous | Catalyst different phase (usually solid) | Fe in Haber; V₂O₅ in Contact; Ni in oil hydrogenation; Pt/Pd/Rh converters |
| Enzyme | Biological (active site) | Carbonic anhydrase, catalase, urease |
| Autocatalysis | Product catalyzes the reaction | $Mn^{2+}$ in $KMnO_4$–oxalic acid |
Heterogeneous mechanism (3 steps): Adsorption → Surface reaction → Desorption. Activity $\propto$ surface area.
Enzyme Kinetics — Michaelis–Menten
$$\boxed{v = \frac{V_{max}[S]}{K_M + [S]}}$$When $[S] = K_M$, $v = \tfrac{1}{2}V_{max}$.
Key Equations at a Glance
| Topic | Headline formula |
|---|---|
| Unique rate | $r = -\frac{1}{a}\frac{d[A]}{dt} = +\frac{1}{c}\frac{d[C]}{dt}$ |
| Rate law | $r = k[A]^m[B]^n$ |
| Zero order | $[A]_t = [A]_0 - kt$, $\ t_{1/2}=\frac{[A]_0}{2k}$ |
| First order | $k=\frac{2.303}{t}\log\frac{[A]_0}{[A]_t}$, $\ t_{1/2}=\frac{0.693}{k}$ |
| Second order | $\frac{1}{[A]_t}=\frac{1}{[A]_0}+kt$, $\ t_{1/2}=\frac{1}{k[A]_0}$ |
| Mean life | $\tau = \frac{1}{k} = 1.443\,t_{1/2}$ |
| Arrhenius | $k = A e^{-E_a/RT}$ |
| Two-temperature | $\ln\frac{k_2}{k_1}=\frac{E_a}{R}\left(\frac{1}{T_1}-\frac{1}{T_2}\right)$ |
| Energy profile | $\Delta H = E_{a,f} - E_{a,r}$ |
| Catalyst boost | $\frac{k_{cat}}{k_{uncat}} = e^{-(E_{a,cat}-E_{a,uncat})/RT}$ |
| Michaelis–Menten | $v = \frac{V_{max}[S]}{K_M+[S]}$ |