Chemical Kinetics

Why does a matchstick flare into flame the instant it is struck, while an iron nail sitting in the open takes months to turn to rust? Why does food spoil in days on the kitchen counter but keep for weeks in a freezer? Thermodynamics can tell you whether a reaction is even allowed to happen at all — whether ΔG\Delta G is negative — and chemical equilibrium can tell you how far it will go before it stops. Neither one says a single word about how fast. That question belongs to a separate branch of chemistry entirely: chemical kinetics, the study of reaction rates and the step-by-step pathways, or mechanisms, by which reactants become products. This chapter builds kinetics from the ground up, in the order a rate experiment would force on you. We start by defining the rate of a reaction precisely — average rate over an interval and instantaneous rate at an instant. We then ask what controls that rate, arriving at the experimentally determined rate law, rate constant kk, and order of a reaction, carefully distinguished from molecularity, which applies only to single-step elementary reactions. From there we integrate the differential rate laws for zero order and first order reactions into equations connecting concentration to time, deriving the characteristic half-life of each. Finally we turn to why temperature so dramatically accelerates reactions, building the Arrhenius equation k=Ae−Ea/RTk = Ae^{-E_a/RT} from the idea of an energy barrier, and finishing with collision theory, effective collisions, and how a catalyst quietly lowers that barrier. By the end you will compute a rate constant from raw concentration-time data, tell order from molecularity without hesitation, apply the integrated rate laws under exam pressure, and use the Arrhenius equation to predict how a reaction speeds up with temperature — the exact toolkit CBSE boards and JEE/NEET test most heavily here.

Key takeaways
  • Rate of reaction is the change in concentration of a reactant or product per unit time; average rate over an interval is −Δ[R]/Δt-\Delta[R]/\Delta t or +Δ[P]/Δt+\Delta[P]/\Delta t, and instantaneous rate is the same expression as Δt→0\Delta t \to 0, i.e. −d[R]/dt-d[R]/dt.
  • The rate law is experimental, not stoichiometric. For Rate=k[A]x[B]y\text{Rate} = k[A]^x[B]^y, the exponents xx and yy must be measured; they need not equal the balanced-equation coefficients aa and bb.
  • Order is the sum of the exponents in the rate law (x+yx + y), can be zero, a whole number, or a fraction, and applies to any reaction, elementary or complex.
  • Molecularity is the number of colliding species in a single elementary step, is always a positive integer from 1 to 3, and has no meaning for a complex (multi-step) reaction as a whole.
  • Zero order: [R]=[R]0−kt[R] = [R]_0 - kt, a straight line of [R][R] against tt with slope −k-k; half-life t1/2=[R]0/2kt_{1/2} = [R]_0/2k depends on starting concentration.
  • First order: k=2.303tlog⁡[R]0[R]k = \dfrac{2.303}{t}\log\dfrac{[R]_0}{[R]}, a straight line of log⁡[R]\log[R] against tt; half-life t1/2=0.693/kt_{1/2} = 0.693/k is independent of starting concentration — the single most tested fact in this chapter.
  • The Arrhenius equation, k=Ae−Ea/RTk = Ae^{-E_a/RT}, links the rate constant to activation energy EaE_a and temperature; a 10 K10\ \text{K} rise roughly doubles kk for most reactions.
  • Collision theory refines Arrhenius: Rate=PZABe−Ea/RT\text{Rate} = PZ_{AB}e^{-E_a/RT}, where ZABZ_{AB} is collision frequency and the steric factor PP accounts for the fact that only properly oriented, sufficiently energetic collisions are effective.
  • A catalyst speeds up a reaction by lowering EaE_a through an alternative pathway, without changing ΔG\Delta G or the equilibrium constant, and it accelerates the forward and reverse reactions equally.
  • Key idea: the rate of a reaction is governed by an experimentally determined rate law and rate constant, which the integrated forms for zero and first order turn into concentration-time equations with characteristic half-lives, while the Arrhenius equation and collision theory explain why that rate constant rises steeply with temperature and can be manipulated by a catalyst.
The core insight

The experimentally measured rate law Rate=k[A]x[B]y\text{Rate} = k[A]^x[B]^y integrates, for zero and first order reactions, into [R]=[R]0−kt[R] = [R]_0 - kt and k=(2.303/t)log⁡([R]0/[R])k = (2.303/t)\log([R]_0/[R]) respectively — giving half-lives [R]0/2k[R]_0/2k and 0.693/k0.693/k — while the rate constant itself climbs exponentially with temperature according to the Arrhenius equation k=Ae−Ea/RTk = Ae^{-E_a/RT}, whose molecular basis is collision theory: only collisions with energy at least EaE_a and the correct orientation, out of a total collision frequency ZABZ_{AB}, actually produce product.

What this chapter covers

Chemical kinetics builds in a strict logical sequence, and this article follows the NCERT chapter's own order.

  • Rate of a chemical reaction — average and instantaneous rate, with correct units and the stoichiometric factor.
  • Factors influencing rate — concentration, temperature and catalyst, leading to the rate law.
  • Rate law, rate constant and order — the experimental relationship between rate and concentration.
  • Molecularity, elementary and complex reactions — colliding species, the rate-determining step, and how molecularity differs from order.
  • Integrated rate equations — concentration-time equations for zero and first order, including gas-phase pressure forms.
  • Half-life — the characteristic time for concentration to fall by half, for zero and first order kinetics.
  • Pseudo first order reactions — how excess of one reactant makes a higher-order reaction look first order.
  • Temperature dependence — the Arrhenius equation, activation energy, and the Maxwell-Boltzmann distribution.
  • Effect of a catalyst — an alternate, lower-energy pathway without altering thermodynamics.
  • Collision theory — collision frequency, effective collisions, orientation, and the steric factor.

The core ideas

Average and instantaneous rate of a reaction

Speed, for a moving car, is distance covered per unit time. For a chemical reaction the equivalent idea is change in concentration of a reactant or product per unit time. For the simplest reaction R→PR \to P in a system of constant volume, with [R]1[R]_1 and [R]2[R]_2 the reactant concentrations at times t1t_1 and t2t_2, the average rate over that interval is defined using the decrease in reactant concentration or, equivalently, the increase in product concentration:

rav=−Δ[R]Δt=+Δ[P]Δt,Δt=t2−t1.(1)r_{av} = -\frac{\Delta[R]}{\Delta t} = +\frac{\Delta[P]}{\Delta t}, \qquad \Delta t = t_2 - t_1. \qquad (1)

where: the minus sign in front of Δ[R]/Δt\Delta[R]/\Delta t is essential — Δ[R]\Delta[R] is negative because the reactant is being consumed, and multiplying by −1-1 makes the rate a positive quantity. Units follow directly: concentration in mol L−1\text{mol L}^{-1} and time in seconds give rate as mol L−1s−1\text{mol L}^{-1}\text{s}^{-1}; for gas-phase reactions monitored by partial pressure, units become atm s−1\text{atm s}^{-1}. Average rate is only ever as good as the interval over which it is calculated, and a reaction's rate is not constant — it falls as reactants are used up. Shrinking the interval to zero gives the instantaneous rate:

rinst=−d[R]dt=+d[P]dt,as Δt→0.(2)r_{inst} = -\frac{d[R]}{dt} = +\frac{d[P]}{dt}, \qquad \text{as } \Delta t \to 0. \qquad (2)

where: this is the slope of the tangent to the concentration-time curve at the instant of interest. NCERT's hydrolysis of butyl chloride example shows the difference sharply: the average rate over successive 5050-second windows falls from 1.90×10−41.90\times10^{-4} to 0.40×10−4 mol L−1s−10.40\times10^{-4}\ \text{mol L}^{-1}\text{s}^{-1}, while the instantaneous rate at t=600 st = 600\ \text{s}, read from a tangent, gives a single sharp value of 5.12×10−5 mol L−1s−15.12\times10^{-5}\ \text{mol L}^{-1}\text{s}^{-1}. When stoichiometric coefficients differ from one, each species' rate of change must be divided by its own coefficient before they agree — in 2HI(g)→H2(g)+I2(g)2\text{HI}(g) \to \text{H}_2(g) + \text{I}_2(g), HI disappears twice as fast as H2\text{H}_2 or I2\text{I}_2 appears. The general definition for aA+bB→cC+dDaA + bB \to cC + dD is

Rate=−1ad[A]dt=−1bd[B]dt=+1cd[C]dt=+1dd[D]dt.(3)\text{Rate} = -\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}. \qquad (3)

where: dividing by the stoichiometric coefficient of each species is what makes "the rate of the reaction" a single unambiguous number, regardless of which species you happen to be monitoring in the lab.

Figure
A concentration versus time curve for a reactant showing a chord between two points whose slope gives the average rate over that interval and a tangent line at a single point whose slope gives the instantaneous rate at that instant
Average rate versus instantaneous rate on a concentration-time curve time t concentration of R chord: average rate over t1 to t2 tangent at t: instantaneous rate t1 t2 t rate falls continuously as concentration falls — never a fixed number

Rate law, rate constant and order of a reaction

For the general reaction aA+bB→cC+dDaA + bB \to cC + dD, experiments show that the rate depends on the concentration of one or more reactants, raised to powers that must be found by experiment. This relationship is the rate law:

Rate=k[A]x[B]y,−d[R]dt=k[A]x[B]y.(4)\text{Rate} = k[A]^x[B]^y, \qquad -\frac{d[R]}{dt} = k[A]^x[B]^y. \qquad (4)

where: kk is the rate constant, a proportionality factor characteristic of the reaction at a given temperature, and xx, yy are the powers to which [A][A] and [B][B] must be raised — the order with respect to AA and BB. The overall order is the sum x+yx + y, and it can be zero, an integer, or a fraction; it is never predicted from the balanced equation, only measured. The classic demonstration is 2NO(g)+O2(g)→2NO2(g)2\text{NO}(g) + \text{O}_2(g) \to 2\text{NO}_2(g). Doubling [NO][\text{NO}] at fixed [O2][\text{O}_2] quadruples the rate (0.096→0.384 mol L−1s−10.096 \to 0.384\ \text{mol L}^{-1}\text{s}^{-1}), showing dependence on the square of [NO][\text{NO}]; doubling [O2][\text{O}_2] alone simply doubles the rate, showing first-order dependence on [O2][\text{O}_2]. The rate law is Rate=k[NO]2[O2]\text{Rate} = k[\text{NO}]^2[\text{O}_2], third order overall, and here the exponents happen to match the stoichiometric coefficients. That match is a coincidence, not a rule: for CHCl3+Cl2→CCl4+HCl\text{CHCl}_3 + \text{Cl}_2 \to \text{CCl}_4 + \text{HCl} the measured rate law is Rate=k[CHCl3][Cl2]1/2\text{Rate} = k[\text{CHCl}_3][\text{Cl}_2]^{1/2}, a fractional order no equation-reading could predict. The rate law must always come from experiment. The units of kk change with the overall order nn, since both sides of the rate law must stay dimensionally consistent:

k=Rate[A]x[B]y=concentration×time−1concentrationn=concentration1−n time−1.(5)k = \frac{\text{Rate}}{[A]^x[B]^y} = \frac{\text{concentration} \times \text{time}^{-1}}{\text{concentration}^n} = \text{concentration}^{1-n}\,\text{time}^{-1}. \qquad (5)

where: for zero order (n=0n=0), kk carries units mol L−1s−1\text{mol L}^{-1}\text{s}^{-1}; for first order (n=1n=1), kk is simply s−1\text{s}^{-1}; for second order (n=2n=2), kk carries mol−1L s−1\text{mol}^{-1}\text{L s}^{-1}. Reading units backward instantly identifies order — k=2.3×10−5 L mol−1s−1k = 2.3\times10^{-5}\ \text{L mol}^{-1}\text{s}^{-1} can only be second order, k=3×10−4 s−1k = 3\times10^{-4}\ \text{s}^{-1} only first.

Molecularity, elementary and complex reactions

A balanced chemical equation almost never shows how a reaction actually happens at the molecular level, because most reactions proceed through a sequence of simpler steps rather than in one leap. A reaction occurring in a single step is called an elementary reaction; a sequence of elementary steps that together accomplish the overall transformation is a mechanism, and the overall reaction is then called a complex reaction.

Molecularity is defined only for a single elementary step: the number of reacting species (atoms, ions or molecules) that must collide simultaneously. Decomposition of ammonium nitrite, NH4NO2→N2+2H2O\text{NH}_4\text{NO}_2 \to \text{N}_2 + 2\text{H}_2\text{O}, is unimolecular; dissociation of hydrogen iodide, 2HI→H2+I22\text{HI} \to \text{H}_2 + \text{I}_2, is bimolecular; and 2NO+O2→2NO22\text{NO} + \text{O}_2 \to 2\text{NO}_2 is trimolecular. Simultaneous collisions of four or more molecules are so improbable that higher molecularities are essentially never observed — a reaction that looks like it needs more colliding species, such as KClO3+6FeSO4+3H2SO4→KCl+3Fe2(SO4)3+3H2O\text{KClO}_3 + 6\text{FeSO}_4 + 3\text{H}_2\text{SO}_4 \to \text{KCl} + 3\text{Fe}_2(\text{SO}_4)_3 + 3\text{H}_2\text{O}, must actually proceed through several simpler steps, even though this reaction is experimentally only second order overall. For a multi-step mechanism, the overall rate is set entirely by the slowest step, the rate-determining step (RDS) — exactly as a relay team's speed is set by its slowest runner. The iodide-catalysed decomposition of hydrogen peroxide, 2H2O2→I−2H2O+O22\text{H}_2\text{O}_2 \xrightarrow{\text{I}^-} 2\text{H}_2\text{O} + \text{O}_2, is experimentally first order in both H2O2\text{H}_2\text{O}_2 and I−\text{I}^-, matching a two-step mechanism: H2O2+I−→H2O+IO−\text{H}_2\text{O}_2 + \text{I}^- \to \text{H}_2\text{O} + \text{IO}^- (slow, the RDS), then H2O2+IO−→H2O+I−+O2\text{H}_2\text{O}_2 + \text{IO}^- \to \text{H}_2\text{O} + \text{I}^- + \text{O}_2 (fast). IO−\text{IO}^- is an intermediate, formed and consumed but absent from the overall equation. Order is experimental, can be zero or fractional, and applies to elementary and complex reactions alike; molecularity is theoretical, never zero or fractional, and meaningful only for a single elementary step. For a complex reaction, overall order equals the molecularity of its rate-determining step.

Integrated rate equations: zero order reactions

The differential rate law is awkward to use directly, since it requires a tangent slope at every instant. Integrated rate equations relate concentration directly to elapsed time, so a single concentration measurement at any moment is enough to extract kk. For a zero order reaction, R→PR \to P with Rate=k[R]0=k\text{Rate} = k[R]^0 = k, integration (worked in full below) gives

[R]=[R]0−kt.(6)[R] = [R]_0 - kt. \qquad (6)

where: [R]0[R]_0 is the initial concentration at t=0t=0. This is a straight line of [R][R] against tt, slope −k-k, intercept [R]0[R]_0 — the diagnostic test for zero order kinetics. Zero order behaviour is uncommon, appearing under saturating conditions: decomposition of gaseous ammonia on a hot platinum surface, 2NH3(g)→PtN2(g)+3H2(g)2\text{NH}_3(g) \xrightarrow{\text{Pt}} \text{N}_2(g) + 3\text{H}_2(g), is zero order at high pressure because the catalyst surface is already saturated, so raising [NH3][\text{NH}_3] further cannot speed the reaction up.

Integrated rate equations: first order reactions

For a first order reaction, R→PR \to P with Rate=k[R]\text{Rate} = k[R], the same integration procedure (below, step by step) gives

ln⁡[R]=ln⁡[R]0−ktor equivalentlyk=2.303tlog⁡[R]0[R].(7)\ln[R] = \ln[R]_0 - kt \qquad \text{or equivalently} \qquad k = \frac{2.303}{t}\log\frac{[R]_0}{[R]}. \qquad (7)

where: plotting ln⁡[R]\ln[R] (or log⁡([R]0/[R])\log([R]_0/[R])) against tt gives a straight line, slope −k-k (or k/2.303k/2.303) — the diagnostic test for first order kinetics. The equivalent exponential form is [R]=[R]0e−kt[R] = [R]_0 e^{-kt}, and between any two times k=1t2−t1ln⁡[R]1[R]2k = \dfrac{1}{t_2-t_1}\ln\dfrac{[R]_1}{[R]_2}, without ever needing [R]0[R]_0. For a first order gas-phase reaction A(g)→B(g)+C(g)A(g) \to B(g) + C(g) monitored by total pressure, if pip_i is the initial pressure and xx the drop in partial pressure of AA at time tt, then pt=pi+xp_t = p_i + x (one mole each of B,CB, C appears per mole of AA lost), so pA=2pi−ptp_A = 2p_i - p_t, giving

k=2.303tlog⁡pi2pi−pt.(8)k = \frac{2.303}{t}\log\frac{p_i}{2p_i - p_t}. \qquad (8)

where: this is the concentration form of equation (7) in disguise, since partial pressure is proportional to concentration; it lets kinetics be followed by a manometer, convenient for decompositions such as N2O5(g)→2NO2(g)+12O2(g)\text{N}_2\text{O}_5(g) \to 2\text{NO}_2(g) + \tfrac{1}{2}\text{O}_2(g). Hydrogenation of ethene and all radioactive decay also obey first order kinetics.

orderdifferential rate lawintegrated rate lawstraight line plothalf-lifeunits of k
zerod[R]/dt=−kd[R]/dt = -kkt=[R]0−[R]kt = [R]_0 - [R][R][R] vs tt[R]0/2k[R]_0/2kmol L−1s−1\text{mol L}^{-1}\text{s}^{-1}
firstd[R]/dt=−k[R]d[R]/dt = -k[R]kt=ln⁡([R]0/[R])kt = \ln([R]_0/[R])ln⁡[R]\ln[R] vs tt0.693/k0.693/ks−1\text{s}^{-1}

Half-life of a reaction

The half-life, t1/2t_{1/2}, is the time needed for a reactant's concentration to fall to exactly half its initial value. For a zero order reaction, substituting [R]=[R]0/2[R] = [R]_0/2 at t=t1/2t = t_{1/2} into equation (6) gives

t1/2=[R]02k,(9)t_{1/2} = \frac{[R]_0}{2k}, \qquad (9)

where: t1/2t_{1/2} is directly proportional to starting concentration for a zero order reaction — halve [R]0[R]_0 and the half-life halves too. For a first order reaction, the same substitution into equation (7) gives the far more famous result

t1/2=0.693k,(10)t_{1/2} = \frac{0.693}{k}, \qquad (10)

where: the half-life of a first order reaction is completely independent of initial concentration — it depends on kk alone. This is the fastest experimental test for first order behaviour: if repeated halvings always take the same time no matter where the clock starts, the reaction is first order.

Pseudo first order reactions

Some reactions that are genuinely second order (or higher) behave experimentally as first order because one reactant is present in such large excess that its concentration barely changes. Ethyl acetate hydrolysis, CH3COOC2H5+H2O→CH3COOH+C2H5OH\text{CH}_3\text{COOC}_2\text{H}_5 + \text{H}_2\text{O} \to \text{CH}_3\text{COOH} + \text{C}_2\text{H}_5\text{OH}, is truly second order, but with water as solvent in vast excess (say 10 mol10\ \text{mol} against 0.01 mol0.01\ \text{mol} ester), its concentration is essentially unchanged, and the rate law collapses to Rate=k′[CH3COOC2H5]\text{Rate} = k'[\text{CH}_3\text{COOC}_2\text{H}_5], apparently first order. Such reactions are pseudo first order reactions; acid-catalysed inversion of cane sugar into glucose and fructose is the other classic example, again first order only because water is in enormous excess.

Temperature dependence of the rate: the Arrhenius equation

Most reactions speed up sharply as temperature rises — a rule of thumb states that the rate constant roughly doubles for every 10 ∘C10\,^{\circ}\text{C} rise near room temperature. The precise relationship, first proposed by van't Hoff and given physical justification by the Swedish chemist Svante Arrhenius, is

k=Ae−Ea/RT.(11)k = Ae^{-E_a/RT}. \qquad (11)

where: AA is the Arrhenius factor or pre-exponential factor (related to collision frequency), EaE_a is the activation energy in J mol−1\text{J mol}^{-1} — the minimum extra energy reactant molecules must acquire to react — RR is the gas constant, and TT is absolute temperature in kelvin. Reactant molecules must first form an unstable, high-energy activated complex (transition state) before breaking down into products; EaE_a is the energy needed to reach that barrier's top, and e−Ea/RTe^{-E_a/RT} is the fraction of molecules energetic enough to clear it.

Figure
A potential energy versus reaction coordinate diagram showing reactants rising over an energy barrier to an activated complex at the peak then falling to products with the activation energy marked as the barrier height and a dashed lower path showing how a catalyst reduces the barrier height without changing the energy of reactants or products
Potential energy profile: activation energy and the effect of a catalyst reaction coordinate potential energy reactants products activated complex Ea (uncatalysed) Ea (catalysed, lower) a catalyst opens a new pathway with lower Ea; reactant and product energies are unchanged

Taking the natural log of equation (11) gives ln⁡k=−Ea/RT+ln⁡A\ln k = -E_a/RT + \ln A, so a plot of ln⁡k\ln k against 1/T1/T is a straight line of slope −Ea/R-E_a/R and intercept ln⁡A\ln A. Writing this at two temperatures and subtracting (full derivation below) gives the two-point form used constantly in numericals:

log⁡k2k1=Ea2.303 R(1T1−1T2).(12)\log\frac{k_2}{k_1} = \frac{E_a}{2.303\,R}\left(\frac{1}{T_1} - \frac{1}{T_2}\right). \qquad (12)

where: k1k_1 and k2k_2 are rate constants at absolute temperatures T1T_1 and T2T_2. This equation finds EaE_a from any two measured rate constants, or predicts kk at a third temperature once EaE_a is known. The reason temperature matters so much is statistical, not a property of any single molecule. Not every molecule carries the same kinetic energy; the fraction NE/NTN_E/N_T possessing energy EE follows a bell-shaped Maxwell-Boltzmann distribution. Raising temperature shifts the curve's peak higher and, crucially, broadens and flattens it, so a much larger fraction now lies above EaE_a — the molecular reason the rate roughly doubles for a 10 K10\ \text{K} rise: the shaded area beyond EaE_a doubles.

Figure
A Maxwell Boltzmann energy distribution curve showing the fraction of molecules on the vertical axis against kinetic energy on the horizontal axis at two temperatures with the higher temperature curve flatter and shifted to higher energy and the activation energy marked with the shaded area beyond it representing the fraction of molecules able to react
Maxwell-Boltzmann distribution: more molecules clear Ea at higher T kinetic energy E fraction of molecules NE/NT temperature T temperature T + 10 Ea shaded area beyond Ea roughly doubles the hotter curve is flatter and broader, but the total area under each curve is the same

Effect of a catalyst

A catalyst is a substance that speeds up a reaction without itself being permanently consumed, and must never be confused with simply adding more reactant. Manganese dioxide catalysing 2KClO3→MnO22KCl+3O22\text{KClO}_3 \xrightarrow{\text{MnO}_2} 2\text{KCl} + 3\text{O}_2 is a standard board example. The accepted explanation is intermediate complex theory: the catalyst forms a temporary bond with a reactant, giving an intermediate complex that decomposes to release the product and regenerate the catalyst unchanged. The net effect, visible in the energy diagram above, is an alternate pathway with lower activation energy — and since equation (11) shows kk rises steeply as EaE_a falls, even a modest drop in EaE_a produces a large rate increase. Three catalyst facts are exam favourites: it does not alter ΔG\Delta G and cannot make a non-spontaneous reaction spontaneous, it does not change the equilibrium constant (it accelerates forward and reverse reactions equally, so equilibrium is reached faster with unchanged composition), and a substance that decreases rate is not a catalyst at all but an inhibitor.

Collision theory of chemical reactions

Arrhenius's equation works well but does not explain why AA and EaE_a take the values they do. Collision theory, developed by Max Trautz and William Lewis around 1916–1918 from the kinetic theory of gases, supplies that picture. Reactant molecules are treated as hard spheres, reacting only when they collide; the number of collisions per second per unit volume is the collision frequency, ZZ. For a bimolecular reaction A+B→ProductsA + B \to \text{Products}, collision theory gives

Rate=ZAB e−Ea/RT,(13)\text{Rate} = Z_{AB}\,e^{-E_a/RT}, \qquad (13)

where: ZABZ_{AB} is the collision frequency of AA with BB, and e−Ea/RTe^{-E_a/RT} is the fraction of collisions energetic enough to exceed EaE_a (comparing with equation (11), AA is essentially the collision frequency). This form works for atoms and small molecules but overestimates rate for larger ones, since not every energetic collision reacts — the molecules also need the correct orientation to let old bonds break and new bonds form. Collisions with both sufficient energy and correct orientation are effective collisions, and a steric factor PP captures the oriented fraction:

Rate=P ZAB e−Ea/RT.(14)\text{Rate} = P\,Z_{AB}\,e^{-E_a/RT}. \qquad (14)

where: PP is typically less than one. Related is threshold energy = activation energy + energy already possessed by the reacting molecules — the total kinetic energy needed at collision, of which EaE_a is only the extra amount above what molecules already carry. Collision theory has real limits, since treating molecules as featureless spheres ignores structure, but it bridges the empirical Arrhenius equation to a molecular picture of rate.

Derivation AIntegrated rate law and half-life for a zero order reaction

The goal here is to convert the differential statement that a zero order reaction proceeds at a constant rate, independent of how much reactant remains, into an equation connecting concentration directly to elapsed time, and then to extract the reaction's half-life from that equation. This is separation-of-variables calculus applied to the simplest possible rate law, and every other integrated rate law in this chapter follows the same three moves: write the differential law, separate and integrate, then use the initial condition to pin down the constant of integration.

Step 1. Write the differential rate law for R→PR \to P when the reaction is zero order: −d[R]dt=k[R]0=k-\dfrac{d[R]}{dt} = k[R]^0 = k, since any quantity to the power zero is 11. The reactant is consumed at a constant rate kk, however much of it remains.

Step 2. Separate variables, concentration on one side and time on the other: d[R]=−k dtd[R] = -k\,dt. Integrating both sides gives [R]=−kt+I[R] = -kt + I, with II an undetermined constant of integration.

Step 3. Fix II from the initial condition [R]=[R]0[R] = [R]_0 at t=0t = 0: [R]0=−k(0)+I[R]_0 = -k(0) + I, so I=[R]0I = [R]_0. This gives the integrated rate law, [R]=[R]0−kt[R] = [R]_0 - kt, confirming equation (6): a straight line of [R][R] against tt with slope −k-k and intercept [R]0[R]_0.

Step 4. Find the half-life by substituting [R]=[R]0/2[R] = [R]_0/2 at t=t1/2t = t_{1/2}: [R]02=[R]0−k t1/2\dfrac{[R]_0}{2} = [R]_0 - k\,t_{1/2}, giving t1/2=[R]02kt_{1/2} = \dfrac{[R]_0}{2k}. Unlike first order, this half-life is directly proportional to starting concentration — twice as much reactant takes exactly twice as long to fall to half, since the disappearance rate never speeds up or slows down.

Go deeper · Derivation B · 1 minIntegrated rate law and half-life for a first order reaction
Derivation BIntegrated rate law and half-life for a first order reaction

The goal is the same as before but for a reaction whose rate is directly proportional to how much reactant remains — the far more common, far more heavily tested case — pushed one step further by showing why the time to reach 99.9%99.9\% completion always comes out to ten half-lives, regardless of the reaction. As before this is separation of variables followed by an initial-condition substitution, but here concentration appears on both sides of the differential equation before separating.

Step 1. Write the differential rate law: −d[R]dt=k[R]-\dfrac{d[R]}{dt} = k[R]. Rearranging gives d[R][R]=−k dt\dfrac{d[R]}{[R]} = -k\,dt; dividing by [R][R] before integrating is what makes this case more involved than the zero order case above.

Step 2. Integrate both sides. The left side gives a natural logarithm, ∫d[R]/[R]=ln⁡[R]\int d[R]/[R] = \ln[R], so ln⁡[R]=−kt+I\ln[R] = -kt + I.

Step 3. Fix II from [R]=[R]0[R] = [R]_0 at t=0t=0: I=ln⁡[R]0I = \ln[R]_0, giving ln⁡[R]=−kt+ln⁡[R]0\ln[R] = -kt + \ln[R]_0, or ln⁡[R][R]0=−kt\ln\dfrac{[R]}{[R]_0} = -kt. Converting to base-1010 logs (ln⁡x=2.303log⁡x\ln x = 2.303\log x) gives the working form of equation (7): k=2.303tlog⁡[R]0[R]k = \dfrac{2.303}{t}\log\dfrac{[R]_0}{[R]}.

Step 4. Extract the half-life by setting [R]=[R]0/2[R] = [R]_0/2: k=2.303t1/2log⁡2=2.303×0.301t1/2k = \dfrac{2.303}{t_{1/2}}\log 2 = \dfrac{2.303 \times 0.301}{t_{1/2}}, giving t1/2=0.693kt_{1/2} = \dfrac{0.693}{k} — independent of [R]0[R]_0, unlike the zero order case. Pushing the same substitution to 99.9%99.9\% completion, where [R]=0.001[R]0[R] = 0.001[R]_0, gives t99.9%=2.303klog⁡(1000)=6.909kt_{99.9\%} = \dfrac{2.303}{k}\log(1000) = \dfrac{6.909}{k}. Dividing by t1/2=0.693/kt_{1/2} = 0.693/k gives t99.9%/t1/2=9.97≈10t_{99.9\%}/t_{1/2} = 9.97 \approx 10: 99.9%99.9\% completion of any first order reaction always takes almost exactly ten half-lives, since both times scale with the same 1/k1/k.

Go deeper · Derivation C · 1 minThe Arrhenius equation and its two-temperature form
Derivation CThe Arrhenius equation and its two-temperature form

The goal is to turn the single-temperature Arrhenius equation, k=Ae−Ea/RTk = Ae^{-E_a/RT}, which by itself contains two unknowns (AA and EaE_a) and cannot be solved from one measurement of kk, into a two-temperature relation that lets EaE_a be extracted from just two rate constants measured at two different temperatures — exactly the calculation every JEE and NEET Arrhenius numerical demands. The technique is logarithms and elimination, not integration, but it is the algebraic backbone behind every activation-energy problem in this chapter.

Step 1. Take the natural log of k=Ae−Ea/RTk = Ae^{-E_a/RT}: ln⁡(Ae−Ea/RT)=ln⁡A−Ea/RT\ln(Ae^{-E_a/RT}) = \ln A - E_a/RT, so ln⁡k=−EaRT+ln⁡A\ln k = -\dfrac{E_a}{RT} + \ln A — equation (12) in linear form, confirming a plot of ln⁡k\ln k against 1/T1/T is a straight line of slope −Ea/R-E_a/R and intercept ln⁡A\ln A.

Step 2. Write this at temperature T1T_1 (rate constant k1k_1) and T2T_2 (k2k_2), treating AA and EaE_a as fixed: ln⁡k1=−EaRT1+ln⁡A\ln k_1 = -\dfrac{E_a}{RT_1} + \ln A and ln⁡k2=−EaRT2+ln⁡A\ln k_2 = -\dfrac{E_a}{RT_2} + \ln A.

Step 3. Subtract the first from the second. The ln⁡A\ln A terms cancel, leaving ln⁡k2−ln⁡k1=EaR(1T1−1T2)\ln k_2 - \ln k_1 = \dfrac{E_a}{R}\left(\dfrac{1}{T_1} - \dfrac{1}{T_2}\right). This cancellation is the entire point — it eliminates the unknown AA without ever measuring it directly.

Step 4. Convert to base-1010 logs to reach the working form used throughout this chapter: log⁡k2k1=Ea2.303 R(1T1−1T2)\log\dfrac{k_2}{k_1} = \dfrac{E_a}{2.303\,R}\left(\dfrac{1}{T_1} - \dfrac{1}{T_2}\right), exactly equation (12). Given any two of k1k_1, k2k_2, T1T_1, T2T_2, EaE_a, the rest follow by algebra — commonly, two rate constants find EaE_a, which is substituted back into equation (11) to find AA, after which kk can be predicted at any third temperature.

Worked examples

Board level - Rate law and order from initial-rate data (CBSE pattern)

For the reaction 2NO(g)+O2(g)→2NO2(g)2\text{NO}(g) + \text{O}_2(g) \to 2\text{NO}_2(g), the following initial rates were measured at constant temperature. *Experiment 1: [NO]=0.30 mol L−1[\text{NO}] = 0.30\ \text{mol L}^{-1}, [O2]=0.30 mol L−1[\text{O}_2] = 0.30\ \text{mol L}^{-1}, rate =0.096 mol L−1s−1= 0.096\ \text{mol L}^{-1}\text{s}^{-1}. Experiment 2: [NO]=0.60 mol L−1[\text{NO}] = 0.60\ \text{mol L}^{-1}, [O2]=0.30 mol L−1[\text{O}_2] = 0.30\ \text{mol L}^{-1}, rate =0.384 mol L−1s−1= 0.384\ \text{mol L}^{-1}\text{s}^{-1}. Experiment 3: [NO]=0.30 mol L−1[\text{NO}] = 0.30\ \text{mol L}^{-1}, [O2]=0.60 mol L−1[\text{O}_2] = 0.60\ \text{mol L}^{-1}, rate =0.192 mol L−1s−1= 0.192\ \text{mol L}^{-1}\text{s}^{-1}. Find the order with respect to each reactant, the overall order, the rate law, and the rate constant with correct units.*

Step 1. Find the order with respect to NO by comparing Experiments 1 and 2, where [O2][\text{O}_2] is held fixed and [NO][\text{NO}] is doubled: the rate rises from 0.0960.096 to 0.3840.384, a factor of 0.384/0.096=40.384/0.096 = 4. Since 2x=42^x = 4 gives x=2x = 2, the reaction is second order in NO.

Step 2. Find the order with respect to O2\text{O}_2 by comparing Experiments 1 and 3, where [NO][\text{NO}] is held fixed and [O2][\text{O}_2] is doubled: the rate rises from 0.0960.096 to 0.1920.192, a factor of exactly 22. Since 2y=22^y = 2 gives y=1y = 1, the reaction is first order in O2\text{O}_2.

Step 3. Write the rate law and overall order: Rate=k[NO]2[O2]1\text{Rate} = k[\text{NO}]^2[\text{O}_2]^1, so the overall order is 2+1=32 + 1 = 3 — third order, even though the numerical exponents happen to match the stoichiometric coefficients here.

Step 4. Find kk using Experiment 1: k=Rate[NO]2[O2]=0.096(0.30)2(0.30)=0.0960.027=3.56 mol−2L2s−1k = \dfrac{\text{Rate}}{[\text{NO}]^2[\text{O}_2]} = \dfrac{0.096}{(0.30)^2(0.30)} = \dfrac{0.096}{0.027} = 3.56\ \text{mol}^{-2}\text{L}^2\text{s}^{-1}; Experiment 3 confirms the same value: 0.192/0.054=3.560.192/0.054 = 3.56. Answer: order in NO =2= 2, order in O2=1\text{O}_2 = 1, overall order =3= 3, rate law Rate=k[NO]2[O2]\text{Rate} = k[\text{NO}]^2[\text{O}_2], and k=3.56 mol−2L2s−1k = 3.56\ \text{mol}^{-2}\text{L}^2\text{s}^{-1}.

Competitive level (JEE / NEET) - First order half-life and fractional completion

A first order reaction has rate constant k=1.15×10−3 s−1k = 1.15\times10^{-3}\ \text{s}^{-1}. Find (a) the half-life of the reaction, (b) the time for the reaction to be 87.5%87.5\% complete, and (c) the time for a 5 g5\ \text{g} sample of reactant to fall to 3 g3\ \text{g}.

Step 1. Half-life directly from equation (10): t1/2=0.693k=0.6931.15×10−3=602.6 st_{1/2} = \dfrac{0.693}{k} = \dfrac{0.693}{1.15\times10^{-3}} = 602.6\ \text{s}, about 603 s603\ \text{s}.

Step 2. For 87.5%87.5\% completion, exactly 12.5%=1/812.5\% = 1/8 of the reactant remains, i.e. [R]/[R]0=(1/2)3[R]/[R]_0 = (1/2)^3 — precisely three half-lives. So t=3×602.6=1808 st = 3 \times 602.6 = 1808\ \text{s}. Checking with equation (7): t=2.303klog⁡(8)=2003×0.903=1809 st = \dfrac{2.303}{k}\log(8) = 2003 \times 0.903 = 1809\ \text{s}, matching to rounding.

Step 3. For 5 g→3 g5\ \text{g} \to 3\ \text{g}, fraction remaining is [R]/[R]0=3/5=0.6[R]/[R]_0 = 3/5 = 0.6 (mass ratios substitute directly for concentration ratios at fixed volume). From equation (7): t=2003×log⁡(1.667)=2003×0.2218=444 st = 2003 \times \log(1.667) = 2003 \times 0.2218 = 444\ \text{s}. Answer: t1/2≈603 st_{1/2} \approx 603\ \text{s}, time for 87.5%87.5\% completion ≈1808 s\approx 1808\ \text{s} (three half-lives), and time for 5 g5\ \text{g} to fall to 3 g3\ \text{g} is 444 s444\ \text{s}. Timing note: under ninety seconds once you recognise the shortcut. Any fraction remaining that is a clean power of one-half — 1/21/2, 1/41/4, 1/81/8, 1/161/16 — should immediately be read as nn half-lives (n=1,2,3,4n = 1, 2, 3, 4) and multiplied by t1/2t_{1/2}, avoiding the log calculation entirely. Reach for the full logarithmic formula, equation (7), only when the fraction remaining is not a clean power of two, as in part (c).

Competitive level (JEE / NEET) - Arrhenius equation: finding Ea and predicting k at a new temperature

The rate constants of a reaction are k1=0.02 s−1k_1 = 0.02\ \text{s}^{-1} at T1=500 KT_1 = 500\ \text{K} and k2=0.07 s−1k_2 = 0.07\ \text{s}^{-1} at T2=700 KT_2 = 700\ \text{K}. Take R=8.314 J mol−1K−1R = 8.314\ \text{J mol}^{-1}\text{K}^{-1}. Find (a) the activation energy EaE_a, and (b) the rate constant k3k_3 at T3=600 KT_3 = 600\ \text{K}.

Step 1. Apply equation (12): log⁡k2k1=Ea2.303R(1T1−1T2)\log\dfrac{k_2}{k_1} = \dfrac{E_a}{2.303 R}\left(\dfrac{1}{T_1} - \dfrac{1}{T_2}\right). Compute the left side: log⁡(0.07/0.02)=log⁡(3.5)=0.544\log(0.07/0.02) = \log(3.5) = 0.544. Compute the bracket: 1/500−1/700=0.002−0.001429=5.714×10−4 K−11/500 - 1/700 = 0.002 - 0.001429 = 5.714\times10^{-4}\ \text{K}^{-1}.

Step 2. Solve for EaE_a: 0.544=Ea2.303×8.314×5.714×10−4=Ea×5.714×10−419.150.544 = \dfrac{E_a}{2.303 \times 8.314}\times 5.714\times10^{-4} = \dfrac{E_a \times 5.714\times10^{-4}}{19.15}, so Ea=0.544×19.155.714×10−4=18,231 J mol−1≈18.23 kJ mol−1E_a = \dfrac{0.544 \times 19.15}{5.714\times10^{-4}} = 18{,}231\ \text{J mol}^{-1} \approx 18.23\ \text{kJ mol}^{-1}.

Step 3. Predict k3k_3 at T3=600 KT_3 = 600\ \text{K} using k1k_1 and EaE_a in the same two-point formula: log⁡k3k1=Ea2.303R(1T1−1T3)=18,23119.15(1500−1600)=952.1×3.333×10−4=0.3174\log\dfrac{k_3}{k_1} = \dfrac{E_a}{2.303R}\left(\dfrac{1}{T_1} - \dfrac{1}{T_3}\right) = \dfrac{18{,}231}{19.15}\left(\dfrac{1}{500} - \dfrac{1}{600}\right) = 952.1 \times 3.333\times10^{-4} = 0.3174.

Step 4. So k3/k1=100.3174=2.08k_3/k_1 = 10^{0.3174} = 2.08, giving k3=0.02×2.08=0.0415 s−1k_3 = 0.02 \times 2.08 = 0.0415\ \text{s}^{-1}. Cross-check using k2k_2 and T2T_2: log⁡(k3/k2)=952.1×(1/700−1/600)=−0.2267\log(k_3/k_2) = 952.1\times(1/700-1/600) = -0.2267, so k3=0.07×10−0.2267=0.0415 s−1k_3 = 0.07\times10^{-0.2267} = 0.0415\ \text{s}^{-1} — the same answer both ways. Answer: Ea≈18.23 kJ mol−1E_a \approx 18.23\ \text{kJ mol}^{-1} and k3≈0.0415 s−1k_3 \approx 0.0415\ \text{s}^{-1} at 600 K600\ \text{K}. Timing note: about two minutes. The efficient path is Step 1 to Step 2 to get EaE_a once, then reuse the same Ea/2.303RE_a/2.303R constant (here 952.1952.1) for every further temperature prediction rather than recomputing it — and always sanity-check a predicted kk by verifying it lies between k1k_1 and k2k_2 when the new temperature lies between T1T_1 and T2T_2, which instantly catches a sign error in the bracket.

Common traps

The single most common error in this chapter is treating the balanced equation as if it were the rate law — assuming the exponents in Rate=k[A]x[B]y\text{Rate} = k[A]^x[B]^y must equal the stoichiometric coefficients. They coincide only sometimes (as with 2NO+O22\text{NO} + \text{O}_2) and just as often do not (as with CHCl3+Cl2\text{CHCl}_3 + \text{Cl}_2, order 3/23/2, or ester hydrolysis, apparent first order despite being bimolecular); the rate law must always be read off experimental data, never guessed. A close second is confusing order with molecularity. Order is experimental, can be zero or fractional, and describes the reaction as a whole; molecularity is theoretical, always a positive integer from 11 to 33, and has no meaning for a complex, multi-step reaction taken as a whole — only for its individual elementary steps. Students frequently drop the stoichiometric factor when coefficients are unequal, quoting the rate as simply −d[HI]/dt-d[\text{HI}]/dt for 2HI→H2+I22\text{HI} \to \text{H}_2 + \text{I}_2 without dividing by 22. Another frequent slip is forgetting that units of kk depend on order and must be derived, not memorised — writing s−1\text{s}^{-1} for a second order kk immediately signals a wrong order. For integrated rate laws, the most damaging mix-up is applying the first order half-life formula, t1/2=0.693/kt_{1/2} = 0.693/k, to a zero order reaction or vice versa — only the first order half-life is independent of starting concentration. In pseudo first order problems, students forget the true order still governs physically; k′k' is only apparent, proportional to the near-constant concentration of the reactant in excess. In Arrhenius calculations, a very common slip is mixing units of EaE_a (joules versus kilojoules) or forgetting TT must be in kelvin, not Celsius. Finally, students conflate threshold energy with activation energy: threshold energy is the total energy needed at collision (activation energy plus energy the molecules already possess), while EaE_a is only the extra amount above what an average molecule already carries.

You should be able to…

  • Define average rate and instantaneous rate from a concentration-time data set, including the correct sign convention and units.
  • Apply the stoichiometric factor correctly when reactant and product coefficients in a balanced equation are unequal.
  • Write a rate law from experimental initial-rate data and determine the order with respect to each reactant and the overall order.
  • Distinguish order from molecularity crisply, including explaining why molecularity has no meaning for a complex reaction as a whole.
  • Derive and apply the integrated rate equations for zero order and first order reactions, including the gas-phase pressure form.
  • Calculate and interpret half-life for both zero order (concentration-dependent) and first order (concentration-independent) reactions.
  • Recognise a pseudo first order reaction and explain why its apparent order differs from its true order.
  • Use the Arrhenius equation, both in single-temperature form and the two-temperature log form, to find EaE_a, AA, or an unknown rate constant.
  • Explain, using collision theory, why not every molecular collision produces product, distinguishing effective collisions, orientation and the steric factor PP.
  • Explain how a catalyst increases rate without changing ΔG\Delta G or the equilibrium constant of a reaction.

Ask the tutor: if you want to work through more rate-law-from-data problems or practice Arrhenius numericals with three or more temperatures, just ask.

Why is the rate of a reaction always written as a positive quantity even though a reactant's concentration is decreasing?

Because rate is defined as a magnitude describing how fast the reaction proceeds, and a negative number would be a confusing way to express "fast" or "slow." Since Δ[R]\Delta[R] for a reactant is inherently negative, the definition Rate=−Δ[R]/Δt\text{Rate} = -\Delta[R]/\Delta t includes a deliberate minus sign that cancels the reactant's own negative change, leaving a positive number. For a product, Δ[P]\Delta[P] is already positive, so no extra sign is needed. Both expressions, correctly written, give the same positive value for the same reaction at the same instant.

What is the real difference between average rate and instantaneous rate, and which one should I use in a calculation?

Average rate is calculated over a finite interval Δt\Delta t and represents a blended value smoothing over how rate actually changes during that interval — easy to calculate from concentrations at two times, but not the "true" rate at any single moment. Instantaneous rate is the limit as Δt\Delta t shrinks to zero, found from the tangent slope, and is the quantity that actually appears in a rate law. Use average rate when you only have two-point data; use instantaneous rate whenever a rate law, rate constant, or order is being determined.

Why can the order of a reaction be zero or a fraction, but molecularity can never be zero or a fraction?

Order is purely an empirical exponent extracted by fitting rate data to a rate law — nothing stops that fit returning zero (as on a saturated catalyst surface) or a fraction like 1/21/2 or 3/23/2 (from combining several elementary steps). Molecularity, by contrast, counts an actual physical number of colliding molecules in one elementary step, and you cannot have zero molecules colliding or half a molecule colliding. This is exactly why molecularity is restricted to whole numbers from one to three, while order carries no such restriction.

Why does the rate of most reactions roughly double for every ten kelvin rise in temperature?

This follows from the Maxwell-Boltzmann distribution and the Arrhenius equation together. Raising temperature shifts the whole distribution of molecular kinetic energies higher and flattens it, increasing the fraction of molecules at or above EaE_a — for typical activation energies (roughly 5050 to 100 kJ mol−1100\ \text{kJ mol}^{-1}), a 10 K10\ \text{K} rise near room temperature happens to roughly double that fraction. It is a rule of thumb, not a law: reactions with unusually high or low EaE_a deviate substantially, and the true relationship is always the exponential k=Ae−Ea/RTk = Ae^{-E_a/RT}.

If a reaction happens in several steps, how do I know which step controls the overall rate, and how does that connect to order?

The step that controls the overall rate is always the slowest one, the rate-determining step, exactly the way a relay race is decided by its slowest runner. Because no later, faster step can outrun the slow step, the concentration dependence of that slow step becomes the dependence of the whole reaction — so the observed order of a complex reaction equals the molecularity of its rate-determining step. In the iodide-catalysed decomposition of hydrogen peroxide, both steps are bimolecular, but the first (slow) step alone fixes the overall rate law as first order in both H2O2\text{H}_2\text{O}_2 and I−\text{I}^-.

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