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Chemistry Notebook

Rate Laws and Integrated Rate Laws

The rate law describes how the reaction rate depends on theconcentrations of the reacting species.

For a general reaction

aA+bBproducts,aA+bB\rightarrow\text{products},

the reaction rate is defined as

v=1ad[A]dt=1bd[B]dt.v = -\frac{1}{a}\frac{d[A]}{dt} = -\frac{1}{b}\frac{d[B]}{dt}.

An experimentally determined rate law may have the form

v=k[A]α[B]β,v=k[A]^\alpha[B]^\beta,

where α\alpha and β\beta are the reaction orders with respect to AA and BB. The overall reaction order is

n=α+β.n=\alpha+\beta.

Reaction orders are determined experimentally. They do not generally have to be the same as the stoichiometric coefficients in the balanced equation. For an elementary reaction, however, the rate law follows directly from the molecularity of that elementary step.

For an overall rate law

v=k[A]n,v=k[A]^n,

the units of rate are concentration per unit time:

[v]=molL1s1.[v]=\mathrm{mol\,L^{-1}\,s^{-1}}.

Therefore,

[k]=molL1s1(molL1)n,[k] = \frac{\mathrm{mol\,L^{-1}\,s^{-1}}} {(\mathrm{mol\,L^{-1}})^n},

which gives

[k]=(molL1)1ns1.\boxed{ [k] = (\mathrm{mol\,L^{-1}})^{1-n}\mathrm{s^{-1}}. }

For a zero-order reaction,

[k]=molL1s1.[k]=\mathrm{mol\,L^{-1}\,s^{-1}}.

For a first-order reaction,

[k]=s1.[k]=\mathrm{s^{-1}}.

For a second-order reaction,

[k]=Lmol1s1.[k]=\mathrm{L\,mol^{-1}\,s^{-1}}.

For a third-order reaction,

[k]=L2mol2s1.[k]=\mathrm{L^2\,mol^{-2}\,s^{-1}}.

Consider a reaction described by

d[A]dt=k[A]n.-\frac{d[A]}{dt}=k[A]^n.

To obtain concentration as a function of time, separate the concentration and time variables:

d[A][A]n=kdt.\frac{d[A]}{[A]^n}=-k\,dt.

or

[A]nd[A]=kdt.[A]^{-n}d[A]=-k\,dt.

Integrate from the initial concentration [A]0[A]_0 at t=0t=0 to the concentration [A][A] at time tt:

[A]0[A][A]nd[A]=k0tdt.\int_{[A]_0}^{[A]}[A]^{-n}d[A] = -k\int_0^t dt.

For n1n\neq1,

[A]nd[A]=[A]1n1n.\int [A]^{-n}d[A] = \frac{[A]^{1-n}}{1-n}.

Therefore,

[[A]1n1n][A]0[A]=kt.\left[ \frac{[A]^{1-n}}{1-n} \right]_{[A]_0}^{[A]} = -kt.

Expanding the limits,

[A]1n[A]01n1n=kt.\frac{[A]^{1-n}-[A]_0^{1-n}}{1-n} = -kt.

Multiplying by 1n1-n gives

[A]1n[A]01n=(n1)kt.[A]^{1-n}-[A]_0^{1-n} = (n-1)kt.

Hence,

[A]1n=[A]01n+(n1)kt\boxed{ [A]^{1-n} = [A]_0^{1-n}+(n-1)kt }

for n1n\neq1.

The first-order case cannot be obtained by directly substituting n=1n=1 into this expression because the integration then involves [A]1[A]^{-1} and gives a logarithm.

For a zero-order reaction,

d[A]dt=k.-\frac{d[A]}{dt}=k.

Rearranging,

d[A]=kdt.d[A]=-k\,dt.

Integrating from [A]0[A]_0 at t=0t=0 to [A][A] at time tt,

[A]0[A]d[A]=k0tdt.\int_{[A]_0}^{[A]}d[A] = -k\int_0^t dt.

This gives

[A][A]0=kt,[A]-[A]_0=-kt,

and therefore

[A]=[A]0kt.\boxed{ [A]=[A]_0-kt. }

The concentration decreases linearly with time, so a plot of [A][A] against tt has slope k-k.

For the half-life,

[A]=[A]02.[A]=\frac{[A]_0}{2}.

Substituting this into the integrated rate law,

[A]02=[A]0kt1/2.\frac{[A]_0}{2} = [A]_0-kt_{1/2}.

Thus,

kt1/2=[A]02,kt_{1/2} = \frac{[A]_0}{2},

and

t1/2=[A]02k.\boxed{ t_{1/2} = \frac{[A]_0}{2k}. }

The half-life of a zero-order reaction therefore depends on the initial concentration.

Zero-order behavior can occur when another part of the reaction system is saturated. Once all available catalytic sites are occupied, for example, increasing the reactant concentration may no longer increase the rate.

For a first-order reaction,

d[A]dt=k[A].-\frac{d[A]}{dt}=k[A].

Separate the variables:

d[A][A]=kdt.\frac{d[A]}{[A]}=-k\,dt.

Integrating between the initial and final conditions,

[A]0[A]d[A][A]=k0tdt.\int_{[A]_0}^{[A]} \frac{d[A]}{[A]} = -k\int_0^t dt.

Since

d[A][A]=ln[A],\int\frac{d[A]}{[A]}=\ln[A],

we obtain

ln[A]ln[A]0=kt.\ln[A]-\ln[A]_0=-kt.

Using

lnxlny=lnxy,\ln x-\ln y=\ln\frac{x}{y},

the integrated rate law becomes

ln[A][A]0=kt.\boxed{ \ln\frac{[A]}{[A]_0}=-kt. }

Exponentiating both sides,

[A][A]0=ekt,\frac{[A]}{[A]_0}=e^{-kt},

so

[A]=[A]0ekt.\boxed{ [A]=[A]_0e^{-kt}. }

The logarithmic form can also be written as

ln[A]=ln[A]0kt.\ln[A]=\ln[A]_0-kt.

Thus a plot of ln[A]\ln[A] against tt is linear with slope k-k.

For the half-life,

[A]=[A]02.[A]=\frac{[A]_0}{2}.

Substitution gives

ln([A]0/2[A]0)=kt1/2.\ln \left( \frac{[A]_0/2}{[A]_0} \right) = -kt_{1/2}.

Therefore,

ln12=kt1/2.\ln\frac12=-kt_{1/2}.

Since

ln12=ln2,\ln\frac12=-\ln2,

we obtain

t1/2=ln2k.\boxed{ t_{1/2}=\frac{\ln2}{k}. }

The initial concentration disappears from the result, so the half-life of a first-order reaction is constant.

If xx is the fraction of reactant converted,

[A]=[A]0(1x).[A]=[A]_0(1-x).

Using the integrated first-order law,

ln([A]0(1x)[A]0)=kt,\ln \left( \frac{[A]_0(1-x)}{[A]_0} \right) = -kt,

so

ln(1x)=kt.\ln(1-x)=-kt.

Hence,

t=1kln(1x).\boxed{ t=-\frac{1}{k}\ln(1-x). }

For 90%90\% conversion,

x=0.90,x=0.90,

so

t90=1kln(0.10)=ln10k.t_{90} = -\frac{1}{k}\ln(0.10) = \frac{\ln10}{k}.

For 99%99\% conversion,

t99=1kln(0.01)=ln100k=2t90.t_{99} = -\frac{1}{k}\ln(0.01) = \frac{\ln100}{k} = 2t_{90}.

For a second-order reaction involving one reactant,

d[A]dt=k[A]2.-\frac{d[A]}{dt}=k[A]^2.

Separate the variables:

d[A][A]2=kdt.\frac{d[A]}{[A]^2}=-k\,dt.

or

[A]2d[A]=kdt.[A]^{-2}d[A]=-k\,dt.

Integrating,

[A]0[A][A]2d[A]=k0tdt.\int_{[A]_0}^{[A]} [A]^{-2}d[A] = -k\int_0^t dt.

Since

[A]2d[A]=1[A],\int[A]^{-2}d[A] = -\frac{1}{[A]},

we obtain

[1[A]][A]0[A]=kt.\left[ -\frac{1}{[A]} \right]_{[A]_0}^{[A]} = -kt.

Therefore,

1[A]+1[A]0=kt.-\frac{1}{[A]} + \frac{1}{[A]_0} = -kt.

Multiplying by 1-1,

1[A]=1[A]0+kt.\boxed{ \frac{1}{[A]} = \frac{1}{[A]_0}+kt. }

A plot of 1/[A]1/[A] against tt is linear with slope kk.

For the half-life,

[A]=[A]02.[A]=\frac{[A]_0}{2}.

Substitution gives

2[A]0=1[A]0+kt1/2.\frac{2}{[A]_0} = \frac{1}{[A]_0} + kt_{1/2}.

Therefore,

kt1/2=1[A]0,kt_{1/2} = \frac{1}{[A]_0},

and

t1/2=1k[A]0.\boxed{ t_{1/2} = \frac{1}{k[A]_0}. }

Unlike first-order kinetics, the half-life increases as the concentration decreases.

For a third-order reaction involving one reactant,

d[A]dt=k[A]3.-\frac{d[A]}{dt}=k[A]^3.

Separate the variables:

[A]3d[A]=kdt.[A]^{-3}d[A]=-k\,dt.

Integrating,

[A]0[A][A]3d[A]=k0tdt.\int_{[A]_0}^{[A]} [A]^{-3}d[A] = -k\int_0^t dt.

Since

[A]3d[A]=12[A]2,\int[A]^{-3}d[A] = -\frac{1}{2[A]^2},

we obtain

[12[A]2][A]0[A]=kt.\left[ -\frac{1}{2[A]^2} \right]_{[A]_0}^{[A]} = -kt.

Thus,

12[A]2+12[A]02=kt.-\frac{1}{2[A]^2} + \frac{1}{2[A]_0^2} = -kt.

Multiplying by 2-2 gives

1[A]2=1[A]02+2kt.\boxed{ \frac{1}{[A]^2} = \frac{1}{[A]_0^2}+2kt. }

For the half-life,

[A]=[A]02.[A]=\frac{[A]_0}{2}.

Therefore,

4[A]02=1[A]02+2kt1/2.\frac{4}{[A]_0^2} = \frac{1}{[A]_0^2} + 2kt_{1/2}.

Hence,

3[A]02=2kt1/2,\frac{3}{[A]_0^2} = 2kt_{1/2},

and

t1/2=32k[A]02.\boxed{ t_{1/2} = \frac{3}{2k[A]_0^2}. }

For n1n\neq1,

[A]1n=[A]01n+(n1)kt.[A]^{1-n} = [A]_0^{1-n}+(n-1)kt.

At the half-life,

[A]=[A]02.[A]=\frac{[A]_0}{2}.

Substitution gives

([A]02)1n=[A]01n+(n1)kt1/2.\left( \frac{[A]_0}{2} \right)^{1-n} = [A]_0^{1-n} + (n-1)kt_{1/2}.

Since

([A]02)1n=[A]01n2n1,\left( \frac{[A]_0}{2} \right)^{1-n} = [A]_0^{1-n}2^{n-1},

we have

[A]01n2n1[A]01n=(n1)kt1/2.[A]_0^{1-n}2^{n-1} - [A]_0^{1-n} = (n-1)kt_{1/2}.

Factorizing,

[A]01n(2n11)=(n1)kt1/2.[A]_0^{1-n} \left( 2^{n-1}-1 \right) = (n-1)kt_{1/2}.

Therefore,

t1/2=2n11(n1)k[A]0n1.\boxed{ t_{1/2} = \frac{2^{n-1}-1} {(n-1)k[A]_0^{n-1}}. }

For n=1n=1, the separate first-order result applies:

t1/2=ln2k.\boxed{ t_{1/2}=\frac{\ln2}{k}. }

Reaction orders do not have to be positive integers.

For example,

v=k[A]1/2v=k[A]^{1/2}

is half-order in AA, while

v=k[A][B]1v=k[A][B]^{-1}

is negative first-order in BB.

Such rate laws usually arise from multistep mechanisms. Intermediate concentrations, adsorption equilibria, inhibition, and radical mechanisms can all produce fractional or negative concentration dependences.

A fractional reaction order does not imply that a fractional number of molecules participates in an elementary step. Reaction order is an experimentally observed concentration dependence, whereas molecularity describes an elementary event.

Determining Reaction Order from Initial Rates

Section titled “Determining Reaction Order from Initial Rates”

Suppose

v=k[A]m[B]n.v=k[A]^m[B]^n.

For two experiments in which only [A][A] changes,

v1=k[A]1m[B]nv_1=k[A]_1^m[B]^n

and

v2=k[A]2m[B]n.v_2=k[A]_2^m[B]^n.

Dividing the second equation by the first eliminates kk and [B][B]:

v2v1=k[A]2m[B]nk[A]1m[B]n.\frac{v_2}{v_1} = \frac{k[A]_2^m[B]^n} {k[A]_1^m[B]^n}.

Therefore,

v2v1=([A]2[A]1)m.\frac{v_2}{v_1} = \left( \frac{[A]_2}{[A]_1} \right)^m.

Taking logarithms,

lnv2v1=mln[A]2[A]1.\ln\frac{v_2}{v_1} = m\ln\frac{[A]_2}{[A]_1}.

Hence,

m=ln(v2/v1)ln([A]2/[A]1).\boxed{ m= \frac{\ln(v_2/v_1)} {\ln([A]_2/[A]_1)}. }

The order with respect to BB can be found in the same way:

n=ln(v2/v1)ln([B]2/[B]1).\boxed{ n= \frac{\ln(v_2/v_1)} {\ln([B]_2/[B]_1)}. }

Consider

v=k[A][B].v=k[A][B].

If BB is present in large excess, its concentration changes very little during the reaction:

[B][B]0.[B]\approx[B]_0.

The rate law becomes

v=k[A][B]0.v=k[A][B]_0.

Since kk and [B]0[B]_0 are both constant, they can be combined into a new observed rate constant:

kobs=k[B]0.k_{\mathrm{obs}}=k[B]_0.

Therefore,

v=kobs[A].\boxed{ v=k_{\mathrm{obs}}[A]. }

The reaction is second order according to its complete rate law, but under these conditions the observed kinetics are first order in AA.

More generally, if

v=k[A]m[B]nv=k[A]^m[B]^n

and BB is in large excess,

kobs=k[B]0nk_{\mathrm{obs}}=k[B]_0^n

and

v=kobs[A]m.v=k_{\mathrm{obs}}[A]^m.

Second-Order Reaction with Two Different Reactants

Section titled “Second-Order Reaction with Two Different Reactants”

Consider

A+BPA+B\rightarrow P

with

v=k[A][B].v=k[A][B].

Let the initial concentrations be

[A]0=a[A]_0=a

and

[B]0=b.[B]_0=b.

If an amount xx has reacted,

[A]=ax[A]=a-x

and

[B]=bx.[B]=b-x.

Therefore,

dxdt=k(ax)(bx).\frac{dx}{dt} = k(a-x)(b-x).

Separating variables,

dx(ax)(bx)=kdt.\frac{dx}{(a-x)(b-x)} = k\,dt.

Using partial fractions,

1(ax)(bx)=1ba(1ax1bx).\frac{1}{(a-x)(b-x)} = \frac{1}{b-a} \left( \frac{1}{a-x} - \frac{1}{b-x} \right).

Thus,

1ba0x(1ax1bx)dx=k0tdt.\frac{1}{b-a} \int_0^x \left( \frac{1}{a-x} - \frac{1}{b-x} \right)dx = k\int_0^t dt.

After integration,

1ba[ln(ax)+ln(bx)+lnalnb]=kt.\frac{1}{b-a} \left[ -\ln(a-x)+\ln(b-x) +\ln a-\ln b \right] = kt.

Combining the logarithms gives

kt=1baln[a(bx)b(ax)].\boxed{ kt = \frac{1}{b-a} \ln \left[ \frac{a(b-x)} {b(a-x)} \right]. }

If a=ba=b, then [A]=[B][A]=[B] throughout the reaction and

d[A]dt=k[A]2,-\frac{d[A]}{dt}=k[A]^2,

so the ordinary second-order integrated rate law applies:

1[A]=1[A]0+kt.\frac{1}{[A]} = \frac{1}{[A]_0}+kt.

Determining Reaction Order from Concentration-Time Data

Section titled “Determining Reaction Order from Concentration-Time Data”

The integrated rate laws give different linear relationships.

For zero-order kinetics,

[A]=[A]0kt,[A]=[A]_0-kt,

so [A][A] plotted against tt is linear.

For first-order kinetics,

ln[A]=ln[A]0kt,\ln[A]=\ln[A]_0-kt,

so ln[A]\ln[A] plotted against tt is linear.

For second-order kinetics,

1[A]=1[A]0+kt,\frac{1}{[A]} = \frac{1}{[A]_0}+kt,

so 1/[A]1/[A] plotted against tt is linear.

For third-order kinetics,

1[A]2=1[A]02+2kt,\frac{1}{[A]^2} = \frac{1}{[A]_0^2}+2kt,

so 1/[A]21/[A]^2 plotted against tt is linear.

For a general order n1n\neq1,

[A]1n=[A]01n+(n1)kt.[A]^{1-n} = [A]_0^{1-n}+(n-1)kt.

Reaction order can also be obtained from rate measurements. Starting from

v=k[A]n,v=k[A]^n,

take the logarithm of both sides:

lnv=ln(k[A]n).\ln v = \ln(k[A]^n).

Using logarithm rules,

lnv=lnk+nln[A].\ln v = \ln k+n\ln[A].

This has the form of a straight line,

y=b+mx,y=b+mx,

with

y=lnv,y=\ln v, x=ln[A],x=\ln[A],

and

m=n.\boxed{ m=n. }

Thus the slope of a plot of lnv\ln v against ln[A]\ln[A] gives the reaction order.

  • IUPAC Compendium of Chemical Terminology (Gold Book), entry on reaction order.
  • OpenStax, Chemistry 2e, sections on rate laws and integrated rate laws.
  • Atkins, P.; de Paula, J.; Keeler, J. Atkins’ Physical Chemistry.