Kinetics
Rate-Determining Step
The slowest step in a multi-step reaction sets the speed of all the rest
The rate-determining step (RDS) is the slowest elementary step in a multi-step mechanism — the one with the highest free-energy barrier. Its rate law is the rate law of the whole reaction. Identifying the RDS lets chemists predict rates, fit kinetics data, and decide where to spend optimization effort.
- AliasesRDS, rate-limiting step
- Identified byLargest ΔG‡
- SetsOrder, Ea, kinetics
- Common probesKIE, Hammett, isotope labels
- Modern formulationEnergy-span model
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The bottleneck principle
A multi-step reaction is a chain of elementary steps. The reactants pass through one or more transient intermediates before becoming products. On a free-energy diagram, the path is a series of valleys (intermediates) connected by saddle points (transition states). The valley-to-saddle climbs are not all the same height; one of them is the highest.
ΔG
│ ┌─────TS₁─────┐
│ ╱ ↑ small ╲ ┌─────TS₂─────┐ ←── RDS (largest barrier)
│ ╱ ΔG‡₁ ╲╱ │ ↑ ╲
│ ╱ ↓ \ │ ΔG‡₂ ╲
│ ──┘ ─┤ ↓ ╲
│ R I ╲
│ ╲ ┌─────TS₃─────┐
│ ╲╱ │ ↑ small ╲
│ \ │ ΔG‡₃ ╲
│ ─┤ ↓ ─── P
└─────────────────────────────────────────────────────────────────────────────→
Reaction coordinate
Whichever step has the highest cumulative ΔG‡ — measured from the lowest-energy intermediate that precedes it up to its transition state — is the rate-determining step. Its rate is the rate of the whole sequence, because nothing downstream can outrun it and nothing upstream can save it.
The classic mental model: water flowing through a series of pipes. The narrowest pipe sets the flow. Widening any wider pipe doesn't help; only widening the narrowest one does.
Worked example: NO₂ + CO via two steps
The gas-phase oxidation of CO by NO₂ is a textbook multi-step kinetics problem. Below 500 K, the experimental rate law is:
rate = k_obs · [NO₂]² (zero order in CO!)
The proposed mechanism is two elementary steps:
Step 1 (slow, RDS): NO₂ + NO₂ → NO₃ + NO k₁
Step 2 (fast): NO₃ + CO → NO₂ + CO₂ k₂
Net: NO₂ + CO → NO + CO₂
Because step 1 is rate-determining, the rate of the whole sequence is the rate of step 1:
rate = k₁ · [NO₂]²
which matches experiment. CO does not appear because it never participates in the rate-determining step — it only reacts with the fast intermediate NO₃. This is the diagnostic signature of an RDS: species that don't appear in the rate law are not involved before the RDS.
Above 500 K, step 1 becomes faster relative to step 2, and the RDS switches. The rate law transforms to first-order in NO₂ and first-order in CO. Same chemistry, different RDS, different observed kinetics.
The steady-state approximation
When the intermediate is reactive (short-lived), apply the steady-state approximation: assume its concentration stays small and constant once the reaction reaches its working regime, so d[Int]/dt ≈ 0. This converts a coupled differential-equation problem into algebra.
Worked example — a generic two-step mechanism:
R ⇌ I rate constants k₁ (forward), k₋₁ (reverse)
I → P rate constant k₂
d[I]/dt = k₁·[R] − k₋₁·[I] − k₂·[I] ≈ 0
[I] = k₁·[R] / (k₋₁ + k₂)
rate = k₂·[I] = k₁·k₂·[R] / (k₋₁ + k₂)
Two limits:
- If k₂ ≫ k₋₁ (forward step from I is much faster than reverse): rate = k₁·[R]. Step 1 is rate-determining; the intermediate disappears as fast as it forms.
- If k₂ ≪ k₋₁ (forward step from I is much slower than reverse): rate = (k₁·k₂/k₋₁)·[R] = K_eq·k₂·[R]. Step 2 is rate-determining; the intermediate equilibrates with reactants before slowly converting to products. This is the pre-equilibrium limit.
Both limits give first-order kinetics in [R], but the observed rate constant is different — k₁ vs K_eq·k₂ — and the activation parameters are different. Distinguishing the two requires temperature variation: pre-equilibrium gives Ea_obs = ΔH₁ + ΔH‡₂ (note the ΔH from the equilibrium); steady-state-with-fast-forward gives Ea_obs = ΔH‡₁.
Kinetic vs thermodynamic control
| RDS analysis (kinetics) | Equilibrium analysis (thermodynamics) | |
|---|---|---|
| Question answered | How fast does the reaction go? | How far does it go? |
| Key parameter | ΔG‡ of the RDS | ΔG of the overall reaction |
| Predictions | Rate law, isotope effects, T dependence | K_eq, product ratio at equilibrium |
| Catalyst effect | Lowers ΔG‡ — accelerates | None — does not change K_eq |
| Concentration effect on RDS | Strong — appears in rate law | Shifts equilibrium per Le Châtelier |
| Time dependence | Yes — rate is dC/dt | No — endpoint only |
| Diagnostic | Reactant orders, KIE, Eyring | K_eq from concentration ratio |
The two analyses are independent. A reaction can be thermodynamically favorable (large negative ΔG) but kinetically slow (large ΔG‡); the RDS is what makes it slow. Conversely, a reaction can be kinetically fast but thermodynamically uphill — it just runs out at the equilibrium endpoint.
Experimental diagnostics for the RDS
- Reactant order matches RDS stoichiometry. Order tells you which species cross the RDS barrier. Second order in NO₂ and zero in CO means only NO₂ participates in the RDS.
- Kinetic isotope effect (KIE). Replace an H with a D. If the C–H (or O–H, N–H) bond breaks in the RDS, k_H/k_D is typically 2–8 (primary KIE). If the bond breaks elsewhere or not at all, KIE ≈ 1. KIE is the most direct way to identify which bond cleaves in the RDS.
- Hammett correlation. Plot log(k) against Hammett σ. Slope ρ ≈ +1 to +3 means a negative-charge TS; ρ ≈ −1 to −3 means a positive-charge TS in the RDS.
- Activation parameters from Eyring plot. ΔH‡ and ΔS‡ describe the RDS. A strongly negative ΔS‡ implies a tight, ordered TS; a positive ΔS‡ implies a loose, dissociative TS. These are RDS properties, not whole-reaction properties.
Where RDS thinking matters
- Industrial catalyst design. The Haber–Bosch nitrogen fixation has N₂ dissociation as its RDS on iron catalysts. Replacing iron with ruthenium-based catalysts halves the activation energy of that step; the rest of the cycle was already fast. Catalyst R&D focuses obsessively on the RDS.
- Enzyme rate enhancement. Triose phosphate isomerase has substrate binding as a diffusion-limited RDS, around 10⁸–10⁹ M⁻¹s⁻¹. Enzymes like this are called "kinetically perfect."
The energy-span model
Modern catalysis papers prefer the energy-span model (Kozuch and Shaik, 2008) over the textbook RDS picture. In a catalytic cycle, the relevant quantity is not the highest single barrier but the largest gap between any low-energy intermediate (the resting state) and any high-energy transition state that follows.
δE = max [ G(TS_i) − G(I_j) ] for all j ≤ i
TOF ∝ exp(−δE / RT)
The model predicts turnover frequency directly from the energy diagram and naturally handles RDS switching as conditions change. It resolves debates about whether the RDS is the "highest barrier" or the "slowest step" — they are not always the same.
Common pitfalls
- Confusing rate-determining with thermodynamically uphill. The RDS is the highest-barrier step; it can be exothermic, endothermic, or thermoneutral. Don't conflate ΔG‡ (kinetic) with ΔG (thermodynamic).
- Assuming the RDS is the first step. Sometimes it is, sometimes not. The position of the RDS depends entirely on the energy profile.
- Using stoichiometric coefficients as reaction orders. Reaction order comes from the RDS, not from the balanced overall equation. The Haber process is N₂ + 3 H₂ → 2 NH₃, but the rate law on iron is roughly k·[N₂]·[H₂]^0.5 because the RDS is N₂ dissociation modulated by H₂ adsorption.
- Forgetting to check whether RDS switches. Mechanisms presented as having one RDS in textbooks often have RDS switching as a function of T, P, or concentration. Eyring plots that show curvature are a warning that one approximation is breaking down.
Related concepts and methods
- Steady-state approximation. Intermediate concentration small and constant; valid when intermediates are reactive.
- Pre-equilibrium approximation. A fast reversible step precedes the RDS; valid when that step is much faster than the RDS.
- Energy-span model. Modern replacement for "the RDS" in catalytic cycles.
- Michaelis–Menten kinetics. Steady-state on the enzyme-substrate complex; RDS shifts between binding and catalysis with substrate concentration.
Frequently asked questions
Is the rate-determining step always the slowest step?
Yes, in the precise kinetic sense: the step with the largest effective barrier (highest ΔG‡) under the experimental concentrations. But 'slow' depends on conditions. A step that is rate-determining at 1 mM substrate may be replaced by a different RDS at 1 M because the apparent rate of any step depends on concentrations of its reactants. The energy span model (Kozuch–Shaik) generalizes this: the RDS is the step with the largest energy span between the lowest preceding intermediate and the highest following transition state.
What is the steady-state approximation?
Assume that any reactive intermediate is consumed as quickly as it forms, so its concentration is small and approximately time-independent: d[Int]/dt ≈ 0. Solve for [Int] in terms of stable species and substitute back into the rate law for the product-forming step. The result is a closed-form rate expression in observable concentrations. Works whenever the intermediate's lifetime is much shorter than the timescale of substrate change.
When is pre-equilibrium the right approximation?
When a fast forward-and-reverse step precedes a slow rate-determining step. The fast step reaches equilibrium long before the RDS depletes the intermediate, so [Int] is set by the equilibrium constant K_eq of the fast step. Substitute [Int] = K_eq·[reactants] into the RDS rate. This gives a different functional form than steady state — typically with K_eq·k_RDS rolled into one observed rate constant.
How do you experimentally identify the RDS?
Compare reactant orders to mechanism predictions; isotope-label the bond suspected to break in the RDS and look for kinetic isotope effects (kH/kD ≈ 2–8 if that bond breaks in the RDS); vary substituents and look for a Hammett correlation that matches the RDS step's polarity; inspect Eyring activation parameters (the RDS sets ΔH‡ and ΔS‡); and measure pre-equilibrium constants for non-rate-determining steps to subtract them out.
Can the rate-determining step change with conditions?
Yes — RDS switching is common. A nucleophilic substitution may have ionization as the RDS at low nucleophile concentration (SN1) and nucleophilic attack as the RDS at high concentration (SN2). Catalytic cycles often shift RDS as the catalyst loading or substrate concentration changes. The change is visible in kinetic data as a curved Eyring plot or a change in observed reaction order.
Why isn't there a single RDS in some mechanisms?
If two steps have very similar barriers, neither dominates and the rate law contains both. The cleanest 'one RDS, others fast' picture is a textbook idealization. Modern catalysis papers report 'energy span' analyses that compute an effective ΔG‡ from all relevant steps; the closer two steps are in energy, the further the system is from a clean single-RDS regime.