Reaction Orders, Integrated Rate Laws, and Half-Life

Reaction Orders

  • Individual Reaction Order: Describes how the rate of a reaction depends on the concentration of a specific reactant.

  • For a simple reaction AproductsA \rightarrow \text{products}, its order with respect to reactant A is determined by how its rate changes when [A][A] changes:

    • First Order with respect to A: If the rate doubles when [A][A] doubles, the rate depends on [A]1[A]^1.

    • Second Order with respect to A: If the rate quadruples when [A][A] doubles, the rate depends on [A]2[A]^2.

    • Zero Order with respect to A: If the rate does not change when [A][A] doubles, the rate does not depend on [A][A] (i.e., depends on [A]0[A]^0).

Graphical Representation of Reaction Orders

  • Plots of Reactant Concentration, [A][A], versus Time: These graphs (visualized in Figure 16.8) show distinct curves for first-, second-, and zero-order reactions, illustrating the rate of decrease in reactant concentration over time.

  • Plots of Rate versus Reactant Concentration, [A][A]: These graphs (visualized in Figure 16.9) depict the direct relationship between reaction rate and reactant concentration for different reaction orders.

Individual and Overall Reaction Orders

  • For a general reaction, such as 2NO(g)+2H<em>2(g)N</em>2(g)+2H2O(g)2NO(g) + 2H<em>2(g) \rightarrow N</em>2(g) + 2H_2O(g), the rate law is experimentally determined.

    • Example: Rate=k[NO]2[H2]1Rate = k[NO]^2[H_2]^1

    • Individual Orders:

      • Second order with respect to NO (exponent of [NO][NO] is 2).

      • First order with respect to H<em>2H<em>2 (exponent of [H</em>2][H</em>2] is 1).

    • Overall Order: The sum of the individual orders (2+1=32 + 1 = 3), making this reaction third order overall.

  • Important Principle: Reaction orders must be determined from experimental data and cannot be deduced from the stoichiometric coefficients in the balanced chemical equation. For instance, H2H_2 has a coefficient of 2 in the balanced equation but a first-order dependence in the rate law.

Problem Solving: Determining Reaction Orders from Rate Laws (Sample Problem 16.2)

  • Problem: Given a rate law, determine the reaction order with respect to each reactant and the overall order. Also, calculate the factor by which the rate changes if concentrations are altered.

  • Plan: Inspect the exponents in the rate law to find individual orders, then sum them for the overall order. For rate changes, substitute the fold-change values into the rate law and calculate.

  • Example (a): For Rate=k[NO]2[O2]Rate = k[NO]^2[O_2]

    • Second order with respect to NO.

    • First order with respect to O2O_2.

    • Third order overall.

    • If [NO][NO] triples and [O<em>2][O<em>2] doubles: Rate new=k(3[NO])2(2[O</em>2])=k(9[NO]2)(2[O<em>2])=18×k[NO]2[O</em>2]=18×Rate oldRate \text{ new} = k(3[NO])^2(2[O</em>2]) = k(9[NO]^2)(2[O<em>2]) = 18 \times k[NO]^2[O</em>2] = 18 \times Rate \text{ old}. The rate increases by a factor of 18.

  • Example (b): For Rate=k[CH3CHO]2Rate = k[CH_3CHO]^2

    • Second order in CH3CHOCH_3CHO.

    • Second order overall.

  • Example (c): For Rate=k[H<em>2O</em>2][I]Rate = k[H<em>2O</em>2][I^-]

    • First order in H<em>2O</em>2H<em>2O</em>2.

    • First order in II^-.

    • Zero order in H+H^+ (since H+H^+ does not appear in the rate law).

    • Second order overall.

Determining Reaction Orders from Experimental Data

  • For a general reaction A+2BC+DA + 2B \rightarrow C + D, the rate law is Rate=k[A]m[B]nRate = k[A]^m[B]^n.

  • Method of Initial Rates: To determine mm and nn, a series of experiments are run where:

    • One reactant's concentration is changed while others are kept constant.

    • The effect on the initial reaction rate is measured.

  • Example: Reaction between O<em>2O<em>2 and NONO (2NO(g)+O</em>2(g)2NO<em>2(g)2NO(g) + O</em>2(g) \rightarrow 2NO<em>2(g), with rate law Rate=k[NO]n[O</em>2]mRate = k[NO]^n[O</em>2]^m).

    • Finding mm (order with respect to O2O_2):

      • Compare experiments where [NO][NO] is constant, but [O2][O_2] changes (e.g., experiments 1 and 2 from Table 16.1).

      • If [O<em>2][O<em>2] doubles and the rate doubles, then 2m=2    m=12^m = 2 \implies m = 1. The reaction is first order with respect to O</em>2O</em>2.

      • Mathematically: racRate<em>2Rate</em>1=rack[NO]<em>2n[O</em>2]<em>2mk[NO]</em>1n[O<em>2]</em>1m=rac[O<em>2]</em>2m[O<em>2]</em>1m=(rac[O<em>2]</em>2[O<em>2]</em>1)mrac{\text{Rate}<em>2}{\text{Rate}</em>1} = rac{k[NO]<em>2^n[O</em>2]<em>2^m}{k[NO]</em>1^n[O<em>2]</em>1^m} = rac{[O<em>2]</em>2^m}{[O<em>2]</em>1^m} = \bigg( rac{[O<em>2]</em>2}{[O<em>2]</em>1}\bigg)^m

      • Solving for mm: m=raclog(Rate<em>2/Rate</em>1)log([O<em>2]</em>2/[O<em>2]</em>1)m = rac{\log(\text{Rate}<em>2/\text{Rate}</em>1)}{\log([O<em>2]</em>2/[O<em>2]</em>1)}. This is useful if the exponent is not easily found by inspection.

    • Finding nn (order with respect to NONO):

      • Compare experiments where [O2][O_2] is constant, but [NO][NO] changes (e.g., experiments 1 and 3).

      • If [NO][NO] doubles and the rate quadruples, then 2n=4    n=22^n = 4 \implies n = 2. The reaction is second order with respect to NO.

  • Types of Reaction Orders: Orders may be positive integers, zero, negative integers, or fractions.

  • Once individual orders are determined, the full rate law can be written (e.g., Rate=k[NO]2[O2]Rate = k[NO]^2[O_2]).

Units of the Rate Constant (k)

  • The value of kk is determined from experimental rate data.

  • The units of kk depend on the overall reaction order.

Information Sequence to Determine Kinetic Parameters (Figure 16.10)

  1. Initial Rates: Obtain initial rates from a series of plots of concentration versus time (by determining the slope of the tangent at t=0t=0 for each plot).

  2. Compare Initial Rates: Compare initial rates when one reactant concentration changes and others are held constant.

  3. Reaction Orders: Determine individual reaction orders (m,nm, n).

  4. Rate Constant (k) and Actual Rate Law: Substitute initial rates, orders, and concentrations into the general rate law (Rate=k[A]m[B]nRate = k[A]^m[B]^n) and solve for kk. This also reveals the actual rate law.

Problem Solving: Determining Reaction Orders & Rate Constants (Sample Problem 16.3)

  • Problem: Use given initial rate data for NO<em>2(g)+CO(g)NO(g)+CO</em>2(g)NO<em>2(g) + CO(g) \rightarrow NO(g) + CO</em>2(g) to find individual and overall reaction orders, calculate kk, and then find the rate for new concentrations.

  • Plan: (a) Use ratios of rate laws from experiments to find mm and nn. (b) Substitute data from one experiment and calculated orders into the rate law to solve for kk. (c) Use calculated kk and new concentrations to find the rate.

  • Solution (a):

    • Order in NO<em>2NO<em>2 (mm): Compare experiments 1 and 2 ([CO][CO] is constant). If [NO</em>2][NO</em>2] quadruples (from 0.10 M to 0.40 M) and the rate increases by a factor of 16 (0.0050 to 0.080 M/s), then 4m=16    m=24^m = 16 \implies m = 2. The reaction is second order in NO2NO_2.

    • Order in CO (nn): Compare experiments 1 and 3 ([NO2][NO_2] is constant). If [CO][CO] doubles (0.10 M to 0.20 M) and the rate does not change (0.0050 M/s), then 2n=1    n=02^n = 1 \implies n = 0. The reaction is zero order in CO.

    • Rate Law: Rate=k[NO<em>2]2[CO]0=k[NO</em>2]2Rate = k[NO<em>2]^2[CO]^0 = k[NO</em>2]^2.

    • Overall Order: 2+0=22 + 0 = 2 (second order overall).

  • Solution (b) - Calculating k (using Experiment 1 data):

    • 0.0050 mol/Ls=k(0.10 mol/L)20.0050 \text{ mol/L} \cdot \text{s} = k(0.10 \text{ mol/L})^2

    • k=rac0.0050 mol/Ls(0.10 mol/L)2=rac0.0050 mol/Ls0.0100 mol2/L2=0.50 L/molsk = rac{0.0050 \text{ mol/L} \cdot \text{s}}{(0.10 \text{ mol/L})^2} = rac{0.0050 \text{ mol/L} \cdot \text{s}}{0.0100 \text{ mol}^2/\text{L}^2} = 0.50 \text{ L/mol} \cdot \text{s}.

  • Solution (c) - Finding rate at new concentrations:

    • Rate=(0.50 L/mols)(0.65 mol/L)2=0.21 mol/LsRate = (0.50 \text{ L/mol} \cdot \text{s})(0.65 \text{ mol/L})^2 = 0.21 \text{ mol/L} \cdot \text{s}(when [NO2]=0.65 M[NO_2] = 0.65 \text{ M} and [CO]=0.25 M[CO] = 0.25 \text{ M}).

Problem Solving: Determining Reaction Orders from Molecular Scenes (Sample Problem 16.4)

  • Problem: Given molecular scenes representing starting mixtures for experiments, determine reaction orders, write the rate law, and predict an initial rate.

  • Plan: (a) Count particles (representing concentrations) and observe rate changes between experiments to determine orders. (b) Write the rate law using determined orders. (c) Use the rate law and particle counts for a new experiment to predict its rate.

  • Solution (a): For reaction A+BproductsA + B \rightarrow \text{products}, with rate law Rate=k[A]x[B]yRate = k[A]^x[B]^y

    • Order with respect to A (red): Compare Expts 1 (2 A, 2 B, Rate = 0.060) and 2 (4 A, 2 B, Rate = 0.120). When [A][A] doubles, Rate doubles (2x=22^x = 2), so x=1x=1. First order with respect to A.

    • Order with respect to B (blue): Compare Expts 1 (2 A, 2 B, Rate = 0.060) and 3 (2 A, 4 B, Rate = 0.240). When [B][B] doubles, Rate quadruples (2y=42^y = 4), so y=2y=2. Second order with respect to B.

    • Overall Order: 1+2=31 + 2 = 3 (third order overall).

  • Solution (b) - Writing the rate law: Rate=k[A][B]2Rate = k[A][B]^2

  • Solution (c) - Predicting initial rate of Expt 4: Compare Expts 3 (2 A, 4 B, Rate = 0.240) and 4 (4 A, 4 B). [A][A] doubles, while [B][B] is constant. Since the reaction is first order in A, the rate doubles. Rate<em>4=2×Rate</em>3=2×0.240=0.480Rate<em>4 = 2 \times Rate</em>3 = 2 \times 0.240 = 0.480

Integrated Rate Law for First-Order Reactions

  • An integrated rate law includes time (tt) as a variable, allowing calculation of concentrations at a specific time or the time required for a concentration change.

  • Differential Rate Law: Rate=racd[A]dt=k[A]Rate = - rac{d[A]}{dt} = k[A]

  • Integrated Rate Equation (Equation 16.4): $ln[A]<em>t=kt+ln[A]</em>0\$ln[A]<em>t = -kt + \ln[A]</em>0 or $ln[A]<em>t[A]</em>0=kt\$ln \frac{[A]<em>t}{[A]</em>0} = -kt

    • [A]t[A]_t: concentration of A at time tt

    • [A]0[A]_0: initial concentration of A (at t=0t=0)

    • kk: rate constant

Problem Solving: Determining Reactant Concentration After a Given Time in a First-Order Reaction (Sample Problem 16.5)

  • Problem: For cyclobutane (C<em>4H</em>8C<em>4H</em>8) decomposition (C<em>4H</em>82C<em>2H</em>4C<em>4H</em>8 \rightarrow 2C<em>2H</em>4), a first-order reaction with k=87 s1k = 87 \text{ s}^{-1}.

    • (a) If [C<em>4H</em>8]<em>0=2.00 M[C<em>4H</em>8]<em>0 = 2.00 \text{ M}, what is [C</em>4H<em>8]</em>t[C</em>4H<em>8]</em>t after 0.010 s0.010 \text{ s}?

    • (b) How long for 70.0%70.0\% of C<em>4H</em>8C<em>4H</em>8 to decompose?

  • Plan: (a) Use the first-order integrated rate law to solve for [A]t[A]_t. (b) Determine the remaining concentration, then use the integrated rate law to solve for tt.

  • Solution (a):

    • ln[A]<em>t=kt+ln[A]</em>0\ln[A]<em>t = -kt + \ln[A]</em>0

    • ln[C<em>4H</em>8]t=(87 s1)(0.010 s)+ln(2.00 M)\ln[C<em>4H</em>8]_t = -(87 \text{ s}^{-1})(0.010 \text{ s}) + \ln(2.00 \text{ M})

    • ln[C<em>4H</em>8]t=0.87+0.693=0.177\ln[C<em>4H</em>8]_t = -0.87 + 0.693 = -0.177

    • [C<em>4H</em>8]t=e0.177=0.838 M[C<em>4H</em>8]_t = e^{-0.177} = 0.838 \text{ M} (after taking the antilog).

  • Solution (b):

    • If 70.0%70.0\% decomposes, 30.0%30.0\% remains. So, [A]<em>t=0.300×[A]</em>0=0.300×2.00 M=0.600 M[A]<em>t = 0.300 \times [A]</em>0 = 0.300 \times 2.00 \text{ M} = 0.600 \text{ M}.

    • ln(0.600 M)=(87 s1)t+ln(2.00 M)\ln(0.600 \text{ M}) = -(87 \text{ s}^{-1})t + \ln(2.00 \text{ M})

    • 0.511=87t+0.693-0.511 = -87t + 0.693

    • 1.204=87t    t=0.0138 s-1.204 = -87t \implies t = 0.0138 \text{ s}.

Reaction Half-Life (t1/2t_{1/2})

  • Definition: The time taken for the concentration of a reactant to drop to half its initial value.

  • For a First-Order Reaction (Equation 16.5):

    • Expression: t1/2=racln2k=rac0.693kt_{1/2} = rac{\ln 2}{k} = rac{0.693}{k}.

    • Key characteristic: For a first-order reaction, t<em>1/2t<em>{1/2} does not depend on the starting concentration ([A]</em>0[A]</em>0). It is a constant at a particular temperature.

    • Relationship: Half-life and the rate constant (kk) are inversely proportional.

    • Application: Radioactive decay is a first-order process, and its half-life is a useful indicator of nuclear stability.

  • Visualizing Half-Lives (Figure 16.11): A plot of [N<em>2O</em>5][N<em>2O</em>5] versus time shows that the time interval to halve the concentration remains constant, regardless of the starting concentration for each interval.

Problem Solving: Using Molecular Scenes to Find Quantities at Various Times (Sample Problem 16.6)

  • Problem: Substance A (green) decomposes to B (blue) and C (yellow) in a first-order gaseous reaction. Given molecular scenes at t=0t=0 and t=30.0 st=30.0 \text{ s}, draw a scene at t=60.0 st=60.0 \text{ s}, find kk, and calculate partial pressure of B at t=90.0 st=90.0 \text{ s}.

  • Plan: (a) Determine half-life from given scenes, then predict particle counts at t=60.0 st=60.0 \text{ s} (two half-lives). (b) Calculate kk from t1/2t_{1/2}. (c) Determine particle counts at t=90.0 st=90.0 \text{ s} (three half-lives), calculate mole fraction of B, then its partial pressure.

  • Solution (a) - Molecular Scene at 60.0 s:

    • At t=0t=0: 8 A particles. At t=30.0 st=30.0 \text{ s}: 4 A particles, 4 B, 4 C. Thus, t1/2=30.0 st_{1/2} = 30.0 \text{ s}.

    • At t=60.0 st=60.0 \text{ s} (two half-lives): A will halve again. Number of A particles = 4/2=24/2 = 2. Since each A $\rightarrow$ 1 B + 1 C, the decomposed A (6 particles) will form 6 B and 6 C particles. Added to the existing 4 B and 4 C, there will be 6 B and 6 C particles (from the first half-life) plus 2 B and 2 C (from the second half-life). So, the total number of B is 4+2=64+2=6 and C is 4+2=64+2=6. Ah, if 6 A decompose over two half lives, that means 4 A (from first half) + 2 A (from second half) = 6 A form 6 B + 6 C. So, at t=60s, there are 2 A, 6 B, 6 C particles. Correction from transcript solution: The solution says "particles of A form 6 of B and 6 of C" which results in 2 A, 6 B, 6 C for a total of 14 particles. Initial was 8 A. After one half life: 4 A, 4 B, 4 C (12 particles). After two half lives: 2 A. The 6 A that disappeared form 6 B and 6 C. So, it should be 2 A, 6 B, 6 C.

  • Solution (b) - Finding k: k=racln2t1/2=rac0.69330.0 s=0.0231 s1k = rac{\ln 2}{t_{1/2}} = rac{0.693}{30.0 \text{ s}} = 0.0231 \text{ s}^{-1}.

  • Solution (c) - Partial pressure of B at 90.0 s:

    • At t=90.0 st=90.0 \text{ s} (three half-lives): Number of A particles = 8/23=18/2^3 = 1. The 7 A particles that decomposed formed 7 B and 7 C. So, 1 A, 7 B, 7 C particles globally.

    • Total particles = 1+7+7=151 + 7 + 7 = 15.

    • Mole fraction of B (XBX_B) = racmole Btotal moles=rac715rac{\text{mole B}}{\text{total moles}} = rac{7}{15}.

    • Partial pressure of B (P<em>BP<em>B) = X</em>B×Ptotal=rac715×5.00 atm=2.33 atmX</em>B \times P_{\text{total}} = rac{7}{15} \times 5.00 \text{ atm} = 2.33 \text{ atm}.

Problem Solving: Determining the Half-Life of a First-Order Reaction (Sample Problem 16.7)

  • Problem: Cyclopropane rearranges to propene (first-order reaction) with k=5.4×102 s1k = 5.4 \times 10^{-2} \text{ s}^{-1} at 1000C1000^{\circ}C.

    • (a) What is t1/2t_{1/2}?

    • (b) How long for concentration to reach one-quarter of initial value?

  • Plan: (a) Use the first-order half-life equation. (b) Recognize that one-quarter concentration means two half-lives.

  • Solution (a):

    • t1/2=rac0.693k=rac0.6935.4×102 s1=12.8 st_{1/2} = rac{0.693}{k} = rac{0.693}{5.4 \times 10^{-2} \text{ s}^{-1}} = 12.8 \text{ s}.

  • Solution (b):

    • Reaching one-quarter of the initial value means the concentration has been halved twice. This corresponds to 2×t1/22 \times t_{1/2}.

    • Time = 2×12.8 s=25.6 s2 \times 12.8 \text{ s} = 25.6 \text{ s}.

Integrated Rate Law and Half-Life for Second-Order Reactions

  • For a Second-Order Reaction with one reactant (e.g., AproductsA \rightarrow \text{products}):

    • Differential Rate Law: Rate=racd[A]dt=k[A]2Rate = - rac{d[A]}{dt} = k[A]^2

    • Integrated Rate Equation (Equation 16.6): rac1[A]<em>t=kt+rac1[A]</em>0rac{1}{[A]<em>t} = kt + rac{1}{[A]</em>0}

    • Half-Life (Equation 16.7): t<em>1/2=rac1k[A]</em>0t<em>{1/2} = rac{1}{k[A]</em>0}

    • Key characteristic: For a second-order reaction, t<em>1/2t<em>{1/2} is inversely proportional to the initial reactant concentration ([A]</em>0[A]</em>0). This means t1/2t_{1/2} is not constant but changes as the reaction proceeds and [A][A] decreases.

Problem Solving: Determining for Second-Order Reactions (Sample Problem 16.8)

  • Problem: HI decomposes to H<em>2H<em>2 and I</em>2I</em>2 (second-order) with k=2.4×102 L/molsk = 2.4 \times 10^{-2} \text{ L/mol} \cdot \text{s} at 25C25^{\circ}C.

    • (a) If 0.0100 mol0.0100 \text{ mol} HI in 1.0 L container, how long for [HI][HI] to reach 0.00900 mol/L0.00900 \text{ mol/L}?

    • (b) Calculate t<em>1/2t<em>{1/2} when [HI]</em>0=1.50 mol/L[HI]</em>0 = 1.50 \text{ mol/L} and when [HI]0=0.750 mol/L[HI]_0 = 0.750 \text{ mol/L}.

  • Plan: (a) Use the second-order integrated rate law to solve for tt. (b) Use the second-order half-life expression for each initial concentration.

  • Solution (a):

    • rac1[HI]<em>t=kt+rac1[HI]</em>0rac{1}{[HI]<em>t} = kt + rac{1}{[HI]</em>0}

    • rac10.00900 mol/L=(2.4×102 L/mols)t+rac10.0100 mol/Lrac{1}{0.00900 \text{ mol/L}} = (2.4 \times 10^{-2} \text{ L/mol} \cdot \text{s})t + rac{1}{0.0100 \text{ mol/L}}

    • 111.1 L/mol=(2.4×102 L/mols)t+100.0 L/mol111.1 \text{ L/mol} = (2.4 \times 10^{-2} \text{ L/mol} \cdot \text{s})t + 100.0 \text{ L/mol}

    • 11.1 L/mol=(2.4×102 L/mols)t11.1 \text{ L/mol} = (2.4 \times 10^{-2} \text{ L/mol} \cdot \text{s})t

    • t=rac11.1 L/mol2.4×102 L/mols=4.6×102 st = rac{11.1 \text{ L/mol}}{2.4 \times 10^{-2} \text{ L/mol} \cdot \text{s}} = 4.6 \times 10^{2} \text{ s}.

  • Solution (b):

    • When [HI]<em>0=1.50 mol/L[HI]<em>0 = 1.50 \text{ mol/L}: t</em>1/2=rac1(2.4×102 L/mols)(1.50 mol/L)=28 st</em>{1/2} = rac{1}{(2.4 \times 10^{-2} \text{ L/mol} \cdot \text{s})(1.50 \text{ mol/L})} = 28 \text{ s}.

    • When [HI]<em>0=0.750 mol/L[HI]<em>0 = 0.750 \text{ mol/L}: t</em>1/2=rac1(2.4×102 L/mols)(0.750 mol/L)=56 st</em>{1/2} = rac{1}{(2.4 \times 10^{-2} \text{ L/mol} \cdot \text{s})(0.750 \text{ mol/L})} = 56 \text{ s}.

    • This demonstrates that for a second-order reaction, reducing the initial concentration by half doubles the half-life.

Integrated Rate Law and Half-Life for Zero-Order Reactions

  • For a Zero-Order Reaction (e.g., AproductsA \rightarrow \text{products}):

    • Differential Rate Law: Rate=racd[A]dt=kRate = - rac{d[A]}{dt} = k

    • Integrated Rate Equation (Equation 16.8): [A]<em>t=kt+[A]</em>0[A]<em>t = -kt + [A]</em>0

    • Half-Life: t<em>1/2=rac[A]</em>02kt<em>{1/2} = rac{[A]</em>0}{2k}

    • Key characteristic: For a zero-order reaction, t<em>1/2t<em>{1/2} is directly proportional to the initial reactant concentration ([A]</em>0[A]</em>0). As [A]<em>0[A]<em>0 decreases, t</em>1/2t</em>{1/2} also decreases.

Graphical Method for Finding Reaction Order from Integrated Rate Laws

  • The integrated rate laws can be rearranged into the form of a straight line (y=mx+by = mx + b) to graphically determine the reaction order.

  • First-Order Reactions (Figure 16.12A):

    • Integrated rate law: $ln[A]<em>t=kt+ln[A]</em>0\$ln[A]<em>t = -kt + \ln[A]</em>0

    • Straight-line form: Plot $ln[A]t\$ln[A]_t (y-axis) versus time (tt, x-axis).

    • Slope: k-k

    • Y-intercept: $ln[A]0\$ln[A]_0

    • A linear plot indicates a first-order reaction.

  • Second-Order Reactions (Figure 16.12B):

    • Integrated rate law: rac1[A]<em>t=kt+rac1[A]</em>0rac{1}{[A]<em>t} = kt + rac{1}{[A]</em>0}

    • Straight-line form: Plot rac1[A]trac{1}{[A]_t} (y-axis) versus time (tt, x-axis).

    • Slope: kk

    • Y-intercept: rac1[A]0rac{1}{[A]_0}

    • A linear plot indicates a second-order reaction.

  • Zero-Order Reactions (Figure 16.12C):

    • Integrated rate law: [A]<em>t=kt+[A]</em>0[A]<em>t = -kt + [A]</em>0

    • Straight-line form: Plot [A]t[A]_t (y-axis) versus time (tt, x-axis).

    • Slope: k-k

    • Y-intercept: [A]0[A]_0

    • A linear plot indicates a zero-order reaction.

  • Graphical Determination Example: Decomposition of N<em>2O</em>5N<em>2O</em>5 (Figure 16.13 and Table 16.3):

    • Concentration data for [N<em>2O</em>5][N<em>2O</em>5] at various times is transformed into $ln[N<em>2O</em>5]\$ln[N<em>2O</em>5] and rac1[N<em>2O</em>5]rac{1}{[N<em>2O</em>5]}.

    • By plotting [N<em>2O</em>5][N<em>2O</em>5] vs. tt, $ln[N<em>2O</em>5]\$ln[N<em>2O</em>5] vs. tt, and rac1[N<em>2O</em>5]rac{1}{[N<em>2O</em>5]} vs. tt, the plot that yields a straight line reveals the reaction order.

    • For N<em>2O</em>5N<em>2O</em>5 decomposition, the plot of $ln[N<em>2O</em>5]\$ln[N<em>2O</em>5] versus time gives a straight line, confirming it is a first-order reaction.

Overview of Zero-Order, First-Order, and Simple Second-Order Reactions (Table 16.3)

Kinetic Parameter

Zero Order

First Order

Second Order

Rate Law

rate=krate = k

rate=k[A]rate = k[A]

rate=k[A]2rate = k[A]^2

Units for kk

mol/L\cdots

1/s

L/mol\cdots

Half-Life (t1/2t_{1/2})

rac[A]02krac{[A]_0}{2k}

racln2krac{\ln 2}{k}

rac1k[A]0rac{1}{k[A]_0}

Integrated Rate Law (straight-line form)

[A]<em>t=kt+[A]</em>0[A]<em>t = -kt + [A]</em>0

$ln[A]<em>t=kt+ln[A]</em>0\$ln[A]<em>t = -kt + \ln[A]</em>0

rac1[A]<em>t=kt+rac1[A]</em>0rac{1}{[A]<em>t} = kt + rac{1}{[A]</em>0}

Plot for Straight Line

[A]t[A]_t vs. tt

$ln[A]t\$ln[A]_t vs. tt

rac1[A]trac{1}{[A]_t} vs. tt

Slope

k-k

k-k

kk

Y-intercept

[A]0[A]_0

$ln[A]0\$ln[A]_0

rac1[A]0rac{1}{[A]_0}

Graph Representation

A straight line sloping downwards for [A]t[A]_t vs. tt

A straight line sloping downwards for $ln[A]t\$ln[A]_t vs. tt

A straight line sloping upwards for rac1[A]trac{1}{[A]_t} vs. tt