Chemical Kinetics:

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Rate Law: equation describing the relationship between the reaction rate and concentration of a reactant or reactants. Rate = k[A]m[B]n where k is called the rate ...
Chemical Kinetics: Rates and Mechanisms of Chemical Reactions C.P. Huang University of Delaware 1

Content 1. 2. 3. 4. 5. 6.

Introduction Reaction rate Rate laws Analysis of rate equations Rate theories Reaction mechanisms 1. 2. 3.

Complex Catalysis Chain

7. Reactions in solution 8. Reactions at interface 2

1. INTRODUCTION

3

Objectives

• Chemical Kinetics: study of rates of chemical reactions and mechanisms by which they occur • A reaction may be spontaneous but does not occur at measurable rates

4

Why kinetics • How fast a reaction can take place? • What steps or pathways are involved in any chemical reaction? • How complete is the chemical reaction? • What are the two major factors controlling the outcome of chemical reactions? • Chemical thermodynamics • Chemical kinetics

5

2. REACTION RATE

6

Definition of reaction rate • Rate – change in some variable per unit time Rate

1/time

• Reaction rate – change in concentration per unit time; M/s or mol/(L-s) • Rates are determined by monitoring concentration as a function of time • Rates are negative for reactants and positive quantities for products

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Types of reaction rate • Instantaneous rate – rate at a specific time • Average rate – ∆[A] over a specific time interval • Initial rate – instantaneous rate at t = 0 • Note: Rates and rate laws are not based on stoichiometry!! They must be determined experimentally.

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Factors affecting reaction rate • Kinetics are very difficult to describe from first principles – Structure, elements, behavior • Rate of reaction describes how fast reactants are used up and products are formed • There are 4 basic factors that affect reaction rates – Nature of reactants – Effective concentrations – Temperature – Presence of catalysts – Number of steps

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Nature of reactants: particle size • The degree of intimacy among particles obviously depends on the physical nature of the particles. • Particles in the liquid state are closer than in the solid state. • Likewise, particles in a finely divided solid will be closer than in a chunk of the solid • In both situations, there is a larger surface area available for the reaction to take place • This leads to an increase in rate. The smaller the particles the faster the reaction rates

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Nature of reactants: bonding • Ions react rapidly: Ag+ + Cl- AgCl(s) Very fast • Reactions which involve bond breaking are slower: NH4+ + OCN- OC(NH2)2 • Redox reactions in solutions are slow • Transfer of electrons are faster than those of atoms. • Reactions between covalently bonded molecules are slow: 2 HI(g) H2(g) + I2(g)

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Concentration • For every reaction the particles must come into intimate contact with each other. • High concentrations by definition implies that particles are closer together (than dilute solutions). • So rate increases with concentration. • Surface area – larger surface area increases reaction • Mixing increases interaction • Need to minimized precipitation or colloid formation

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Temperature • Temperature affects rate by affecting the number and energy of collisions • So an increase in temperature will have the effect of increasing reaction rate

13

Reaction rates and stoichiometry • Rate has units of moles per liter per unit time - M s-1, M h-1 • Consider the hypothetical reaction aA + bB  cC + dD 1 [ A] 1 [ B ] • We can write r 

a t b t 1 [C ] 1 [ D]   c t d t

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Example At a given time, the rate of C2H4 reaction is 0.23 M/s. What are the rates of the other reaction components? C2H4(g) + 3 O2(g) → 2 CO2(g) + 2 H2O(g) 0.23 M/s

?

?

?

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3. RATE LAW

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Rate law • Consider the following reaction aA + bB  products • Rate Law: equation describing the relationship between the reaction rate and concentration of a reactant or reactants Rate = k[A]m[B]n where k is called the rate constant

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Concentration and rate aA + bB → cC + dD • General form of rate law: rate = k[A]m[B]n [A], [B] – concentration, in M or P k – rate constant; units vary m, n – reaction orders • Reaction orders and, thus, rate laws must be determined EXPERIMENTALLY!!! – Note: m ≠ a and n ≠ b – Overall order = sum of individual orders 18

Reaction order • Rate = k[A][B]0 m = 1 and n = 0 - reaction is first order in A and zero order in B - overall order = 1 + 0 = 1 - usually written: Rate = k[A] • The values of the reaction order must be determined experimentally; they cannot be found by looking at the equation, i.e., the stoichiometry of the reaction

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Rate law • m, n are called reaction orders - they indicate the sensitivity of the rate to concentration changes of each reactant • NOTE: the orders have nothing to do with the stoichiometric coefficients in the balanced overall equation • An exponent of 0 means the reaction is zero order in that reactant - rate does not depend on the concentration of that reactant

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Rate Law • An exponent of 1, rate is directly proportional to the concentration of that reactant - if concentration is doubled, rate doubles - reaction is first order in that reactant • An exponent of 2, rate is proportional to the square of concentration of that reactant – if concentration is double, rate is quadrupled – reaction is second order in that reactant

• The overall reaction order is the sum of all the orders

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Reaction orders For the reaction: A →B, the rate law is: rate = k[A]m Order (m)

∆[A] by a factor of

Rate increases by

Zero (0)

2, 4, 15, ½, etc.

None

2 3 2 3 ½

2X 3X 4X 9X ¼X

1st

(1)

2nd (2)

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Example 2 NO(g) + 2 H2(g) → N2(g) + 2 H2O(g) rate = k[NO]2[H2] 1. 2. 3. 4. 5. 6.

What is the order with respect to NO? What is the order with respect to H2? 3 What is the overall order?

2 1

If [NO] is doubled, what is the effect on the reaction rate? quadrupled If [H2] is halved, what is the effect on the reaction rate? halved What are the units of k? M-2-s-2 23

Example PtCl2(NH3)2 + H2O  PtCl(H2O)(NH3)2 + Cl-

Calculate the rate of reaction when the concentration of PtCl2(NH3)2 is 2.0x10-2 M. Rate = 9x10-3 (h-1) x 0.02 (M) = 1.8x10-5 (M-h-1)

What is the rate of Cl- production under these conditions? d[Cl]/dt = rate = 1.8x10-5 (M-h-1) 24

Example 2 NO(g) + 2 H2(g) → N2(g) + 2 H2O(g) rate = k[NO]2[H2] k = 6.0 x 104 M-2s-1 @1000K

Calculate rate when [NO] = 0.025 M and [H2] = 0.015 M. Rate = 6x10-4 (M-2-s-1)x0.025 M x 0.015 M =225 (M-s-1)

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Measurement of reaction rate Rate may be measured in three ways • Average reaction rate: a measure of the change in concentration with time • Instantaneous rate: rate of change of concentration at any particular instant during the reaction • Initial rate: instantaneous rate at t = 0; that is, when the reactants are first mixed

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Measurements of reaction rate C C

C Initial rates nc

Instantaneous rate

nc

nt

C1 C2 C3 t

t

t1

t2

t3

t

Here nc is true order, with respect to concentration and nt is order with respect to time. When nt < nc, reaction is inhibitory and when nt >nc reaction is autocatalytic. 27

C4H9Cl(aq) + H2O(l) → C4H9OH(aq) + HCl(aq) Time, s

[C4H9Cl], M

0

0.1000

50

0.0905

100

0.0820

150

0.0741

200

0.0671

300

0.0549

400

0.0448

500

0.0368

800

0.0200

10,000

0

In this reaction, the concentration of butyl chloride, C4H9Cl, is measured at various times.

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Time, s

[C4H9Cl], M

Average rate, M/s

0

0.1000

50

0.0905

1.9E-4

100

0.0820

1.7E-4

150

0.0741

1.6E-4

200

0.0671

1.4E-4

300

0.0549

1.22E-4

400

0.0448

1.01E-4

500

0.0368

0.8E-4

800

0.0200

0.56E-4

10,000

0

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C4H9Cl(aq) + H2O(l) → C4H9OH(aq) + HCl(aq)

Initial rate

Instantaneous rate at 500 s

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Determination of rate law The method of initial rate • Measuring the initial rates as a function of the initial concentrations • Avoids problems of reversible reactions • Initially there are no products so they cannot affect the measured rate • This method is chosen to check the effect of a single reactant on the rate

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Bench-Top Reactors

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Atlas Reactors

http://www.syrris.com/batch-products/atlas-parallel-system

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Stopped-Flow Technique

http://www.hi-techsci.com/techniques/stoppedflow 34

Temperature Jump

http://www.hi-techsci.com/techniques/stoppedflow 35

Quench-Flow Technique

http://www.hi-techsci.com/techniques/stoppedflow

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Summary of Experimental Methods Method

Range of half-life, s

Conventional

102 – 108

Flow

10-3 - 102

Relaxation

10-10 -1

pressure jump

10-6 - 1

temperature jump

10-7 - 1

field pulse

10-10 – 10-3

shock tubes

10-9 – 10-3

Kinetic spectroscopy

10-15 – 10-10

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4. ANALYSIS OF RATE LAW

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Types of rate laws • Differential rate law or rate law: Shows how the reaction rate changes with concentration • Integrated rate law: Shows how concentration changes with time

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First order Log [A]

R

1 d[ A]  k (T ,I )[ A ] ν A dt 1.0

[ A ]  [ A ] o e  k ( T ,I )t k ( T ,I ) log[ A ]  log[ A ] o  t 2.303

0.1

0.01

0.001

t 1

2

3 40

Second order

R 

1 d[ A ]  k ( T )[ A ] 2  A dt

1 1   ν i k ( T )t [A] [ A ]0

  [ A ]o   A [B]o ln B [A] 

  [B]o    ln  A [ A ]o  

    B [B]o   A [ A ]o k(T )t 

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Third order 1 d[ A ] R  k(T )[ A ][B ][C ]  A dt

 A  B  C  1 [ A ]o  [B]o  [C]o

1 1   2k(T )t 2 2 [A] [ A ]o

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Summary Rate Equations Rate = k[A]n; [A] = concentration at time t, [Ao] = initial concentration, [X] = product conc. 0 order

[A0]-[A] = kt, [X] = kt

1st order ln[A ] - ln[A] = kt, 0 2nd order

3rd order

k = M/s ln[A0] - ln([Ao] - [X]) = kt

k = 1/s

k = M-1-s-1

k = M-2-s-1

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Half-life • The half-life, t1/2, is defined as the time it takes for the reactant concentration to drop to half its initial value

• Note: the half-life for a first order reaction does not depend on the initial concentration • The value of the half-life is constant

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Half-Life • Half-life – A =Aoe-t –  = ln2/t1/2 – If a rate half life is known, fraction reacted or remaining can be calculated

(CH3)2N2(g)  N2(g) + C2H6(g) Time Pressure (torr) 0 36.2 30 46.5 t 0

A 36.2 30 36.2(1-x)

B 0 36.2x

C 0 36.2x

46.5 = 36.2(1-x+2x)=36.2(1+x)=36.2+36.2x

Ct =Coe-kt

46.5-36.2 = 36.2x x = 0.285

kt0.5=ln(2) to.5 = - [ln(2) t]/[ln(Ct/Co)]

A = 36.5(1-0.285) = 25.9

to.5 = - [ln(2) (30)]/[ln(25.9/36.5)]=62.1 (min) 45

t0.5 2t0.5 t0.53 t0.5

t0.5

t0.5

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5. RATE THEORY

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ARRHENIUS’ EQUATION • In 1885, Hood proposed the following equation: A' logk  B  T • In 1884, vant’s Hoff-Arrhenius proposed the following equation: d ln K c E  dT RT 2

Kc is the equilibrium constant 48

ARRHENIUS’ EQUATION k1 k 1 A  B   CD

k1[ A][ B]  k 1[C ][ D] Kc 

k1 [C ][ D]  k 1 [ A][ B]

Ea d ln k  dT RT 2 Ea ln k   C RT

d ln k1 E  12 1 dt RT d ln k 1 E  12  1 E  E1  E 1 dt RT d ln k1 d ln k 1 E   dt dt RT 2

C = constant

Activated state; X*

E2 E1 Final state E=Ea

Initial state

49

Arrhenius Equation • Svante Arrhenius developed an equation for the mathematical relationship between k and Ea.

• A is the frequency factor, which represents the number of effective collisions. E  • e RT : Boltzmann expression for the fraction of system having energy in excess of the value, Ea, so that is may be identified with the fraction of reactant molecules that are activated complexes a

50

Arrhenius Equation Or log k = log A –Ea/(2.303 R) (1/T) Slope = Ea/2.303 R = Ea/4.57 Cal

Y=mx+b

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To find slope, m Ln k

m=

 k2  ln    k   1   1 1     T T1    2

Ea/3R

1/T

52

Arrhenius’ Equation • This is Arrhenius’ Equation • Can be arranged in the form of a straight line • ln k = (-Ea/R)(1/T) + ln A • Plot ln k vs. 1/T  slope = -Ea/R Log [k]

EA/2.303 = dlog K/d(1/T)

1.0

Ea < 5 kcal/mol: diffusion control reaction Ea > 5 kcal/mol; reactive control

0.1

Diffusion regime

Reaction regime

0.01

0.001

1/T 1

2

3

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Activation Energy, Ea • Energy barrier (hump) that must be overcome for a chemical reaction to proceed • Activated complex or transition state – arrangement of atoms at the top of the barrier

54

Temperature Effects Maxwell-Boltzmann Distribution

• At higher temperatures, more molecules will have adequate energy to react. • This increases the reaction rate. 55

Example A reaction which rate constant doubles when temperature is raised by 10oK from 300 oK. What is its Ea value? Given k310 = 2k300 or k1 = 2k0 Given k310 = 2k300 or k1 = 2k0 Ea 

k k T1To 310)(300 (8.34) ln o  53594(J / mol) ln 0  2k o T o  T1 k 1 (300  310)

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Summary of A and Ea Reaction

A

Ea(kJ/mol)

N2ON2+O N2O5 2NO+O2 N2+ON+NO OH+H22H2O+H

8x1011 6x1014 1x1011 1x1011

251 88 315 42

1st 1st 2nd 2nd

CO2+OH-HCO3- 1x1011

315

2nd

57

Example It is given for a specific reaction, k =0.00123 /ms at 290oK and 0.0394/ms at 350oK. What is its Ea and k at 308oK? ln k 1  ln A 

Ea RT1

 (350)(298)   0.0394  Ea     57811( J / mol)  57.8(kJ / mol) (8.34 ) 350  298 0 . 00123    

E  1 k 1 ln 2  a    k1 R  T2 T1   TT  k  E a   1 2 R ln 2   T2  T1   k1 

ln k  ln(0.00123 ) 

57811  1 1      8.70  0.578  5.94 8.324  308 298 

k  e 5.94  0.00263  2.63x10 3 (1/ ms)

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Collision Theory • COLLISION THEORY: a reaction results when reactant molecules, which are properly oriented and have the appropriate energy, collide • The necessary energy is the activation energy, Ea

M. Silberberg

59

Molecular Orientation and Effective Collisions • Not all collisions leads to a reaction • For effective collisions proper orientation of the molecules must be possible

60

Molecular Collisions

Before collision

Effective collision

Before collision No-effective collision 61

Collision Theory two identical gas molecules colliding with each other at a velocity, v (molecules/cm3-s) [N.C. Leuis (1918) and Eyring (1935)]

v  z AA e z AA



E RT

zAA = # collision/(s-cm3)

1  2 d 2 cn 2 2 c

molecules/(cm3-s)

8κT = average velocity of each molecule πm

m: mass of each molecules k = Boltzmann constant

1 8 T T 2d2n2  2n2 d2 2 m m 1 E m A  mB  2  RT 2  v  n A nB d AB 8T  e dAB: average distance, sum of radii m A mB   z AA 

62

Collision Theory 1 2

v  n A nB d

k = k’Na (cm3/mol-s)

2 AB

E  m A  mB   RT  e 8T m A mB  

1 2

E    m m  v B RT k'   d 2AB 8T A  e m A mB  n A nB  1 2

E    m m  B RT k  Na d 2AB 8T A  e m A mB   1 2

m A  mB  2  A  Na d AB 8T  Z m A mB   1

k  BT e 2



E RT

B

k  PZe

E  RT

Z T

63

Example Estimate he rate constant for the decomposition of HI(g) molecules at 321.4oC according to the collision theory. Given for the HI(g) molecules the following prosperities: 2HI(g) = H2(g) +I2(g) = 3.5 Å = 3.5x10-8 cm; E = 44,000 cal/g-mol; mA = mB = MHI = 128 g; R = Na = 1.38x10-16x6.023x1023 = 8.3x107 (erg/oK-mol) = 1.98 (cal/oK-g-mol) T = 273 + 321.4 = 594.6 oK

64

Example

1 2

  2    44000 (8.34 x107 )(594.6 ) 7 k'  (3.5 x10 ) 88.3x10 594.6  e  128     1.70x10 10 e  37.4 8 2

 9.72x10  27 (cm 3 / molecules  s)

k =9.72x10-27 (cm3/moleculesx)(6.023x1023)(molecules/mol) = 5.86x10-3 (cm3/mol-s) =5.86x10-3x(1000) =5.85x10-6 (L/mol-s)

65

Example Collision of two water molecules at room temperature, 298 oK, given: d = 0.30 nm, T=298oK; mA=mB=18(g-mol-1)/6.023x1023 =2.99x10-26 kg;  =1.38x10-23 J/oK



Z   0.3x10    9 2



81.38x10

 23

298

 26   2.99x10  / 6x10  2.37x10 10 (cm 3 / molecules  s)  26 2



   

1 2

 2.37x10 16 (m 3 / molecules  s)

66

Example

Reaction

k’ (cm3-molecules-1-s-1)

k (L-mol-1-s-1)

CH4+OHCH3 + H2O

8.14x10-15

4.9x1012

CH3+O2 CH2O+OH

3.76x10-36

2.26x10-9

CH3O+O CH2O+OH

1.7x10-11

1.02x1016

k (L-mol-1-s-1) = 1000 x6.023x1023 k’ (cm3-molecules-1-s-1)

67

Transition State Theory • During a chemical reaction, reactants do not suddenly convert to products • The formation of products is a continuous process of bonding breaking and forming • At some point, a transitional species is formed containing “partial” bonds • This species is called the transition state or activated complex

68

Transition State Theory • The transition state is the configuration of atoms at the maximum of the reaction energy diagram • The activation energy is therefore the energy needed to reach the transition state • Note also that the transition state can go on to form products or break apart to reform the reactants

rA

uA R

b uBC

rB

69

Transition State Theory A + B = AB*  C r = [AB*];  (s-1); [AB*](molecules/cm3) a *AB  *AB [ AB*]  K  a A aB  A B [ A][ B] *

 *AB r  K * [ A][ B ]  A B

K*  e

 G*

K = 1.38x10-16 erg/oK

RT



T



= 6.624x10-27 erg/s

 70

Transiton Theory T   *AB  r    A B

   S * / R   H * / RT   e 

T   *AB  S */ R   e A    A B  T   *AB  S */ R   H */ RT  e r e    A B  

T

f  e S */ R e  H */ RT

  TZe  H */ RT

E =H* 71

Summary of Rate Theory

Rate Theory Arrhenius Collision Activated Complex (Transition)

Equation k  Ae 1 2



k  BT e

Ea



A term RT

E RT

T  S * R  H* RT k e e 

A BT1/2

T  S * R e 

Exponential term Ea RT Ea RT H * RT

72

6. REACTION MECHANISMS

73

Reaction Mechanisms • Reactions occur in a series of elementary steps collectively called a mechanism. • Determining the reaction mechanism is the overall goal of kinetic studies. • One step, the rate-determining step (RDS), is much slower than the other. • Usually, an intermediate (isolable) or a transition state (non-isolable) is formed at some point during the reaction. • molecularity – the number of molecules that participate in a reaction

74

Reaction Mechanism • MECHANISM: the step-by-step pathway by which a reaction occurs • Each step is called an elementary step – NO2(g) + CO(g)  NO(g) + CO2(g) • Mechanism: – NO2(g) + NO2(g)  NO(g) + NO3(g) – NO3(g) + CO(g)  NO2(g) + CO2(g) • NO3 is a reaction intermediate

75

Reaction Mechanism • The slow step is called the ratedetermining step (RDS) or rate-limiting step (RLS) • A reaction can never occur faster than its slowest step • Overall reaction = sum of all elementary steps • The mechanism proposed must be consistent with the rate law

76

Elementary Steps and Molecularity Molecularity

Elementary Reaction

Rate Law

Unimolecular

A  products

Rate = k[A]

Bimolecular

A + A  products

Rate = k[A]2

Bimolecular

A + B  products

Rate = k[A][B]

Trimolecular

A + A + A  products

Rate = k[A]3

Trimolecular

A + A +  products

Rate = k[A]2[B]

Trimolecular

A + B + C  products

Rate = k[A][B][C]

Molecularity is the number of molecules reacting.

77

Steady-state Approach • When reaction mechanism has several steps of comparable rates, the rate-limiting step is often not obvious. There are intermediates in some steps. • SSA: a method used to derive a rate law based on the assumption that one intermediate is consumed as quickly as it is generated. 2 N2O5  4NO2 + O2

N2O5  NO2 + NO3 NO3 + NO2  NO+ NO2 + O2 NO3 + NO  2NO

(1) (2) (3)

78

2N2O5 4NO + O2 N2O5

k1 k-1

NO2 + NO3

NO3 + NO NO3 + NO

k2 k3

NO + NO2 + O2 2NO

d [ NO ]  k 2 [ NO3 ][ NO ]  k3 [ NO3 ][ NO ]  0 dt

k 2 [ NO3 ][ NO2 ] [ NO ]  k3 [ NO3 ] d [ NO3 ]  k1[ N 2O5 ]  k 2 [ NO3 ][ NO2 ]  k3 [ NO3 ][ NO ]  k 1[ NO2 ][ NO3 ]  0 dt

[ NO3 ] 

k1[ N 2O5 ] k 2 [ NO3 ][ NO2 ]  k3[ NO3 ][ NO ]  k 1[ NO2 ][ NO3 ]

79

[ NO3 ] 

k1[ N 2O5 ] k 2 [ NO2 ]  k3 [ NO]  k 1[ NO2 ]



k1[ N 2O5 ] k  (k 2  k 1 )[ NO2 ]  k3  2 [ NO2 ]  k3 



k1[ N 2O5 ] (2k 2  k 1 )[ NO2 ]

d [O2 ]  k 2 [ NO3 ][ NO2 ] dt k k k [ N O ][ NO2 ]  1 2 3 2 5 (2k 2  k 1 )[ NO2 ]

r



k1k 2 k3 [ N 2O5 ]  k '[ N 2O5 ] (2k 2  k 1 ) 80

Catalysis • Catalyst – increases the rate of a reaction without being consumed or changing chemically • Accomplishes this by lowering the activation energy by changing the reaction mechanism. • Heterogeneous vs. homogeneous catalysis • Examples: – Catalytic converter – Enzymes in the body – Ozone depletion

81

Catalysis • Reaction rates are also affected by catalysts • Catalyst: a substance that increases the rate of a reaction without being consumed in the reaction • Catalysts work by providing alternative pathways that have lower activation energies • A catalyst may be homogeneous or heterogeneous • Homogeneous: catalyst and reactants are in the same phase 82

Energy

Ea

Uncatalyzed pathway Catalyzed pathway

Ea

products

E Reactants

Reaction process

83

• Heterogeneous: catalyst in a different phase • Typically: a solid in a liquid • An important example: catalytic converters in automobile - convert pollutants to CO2 H2O, O2, N2 - usually Pt, Pd, V2O5, Cr2O3, CuO • Cars must use unleaded fuels – lead poisons the catalytic bed 84

Enzyme Kinetics Michaelis-Menten mechanism for enzyme kinetics is:

85

Catalytic efficiency,   = kcat/KM  = k2/[(k-1+k2)/k1]   max, = k1; if k2 >>k-1 k1 = rate of formation of ES Diffusion limit ~ 108 – 109 M-1-s-1 For enzyme sized molecules at room temperature Decomposition of hydrogen peroxide  = 4x108 M-1-s-1

Turnover number or catalytic constant = number of catalytic cycles performed by the activate Site in a given time intervals divided by the duration of that

86

Lineweaver Burk Plot

1 KM 1 1   v vmax S  S 

vmax [ S ] v K M  [S ]

S   K M v

vmax



S  vmax

v/[S]

[S]/v

1/v

v vmax v   S  K M K M

1/vmax

KM/vmax

1/KM vmax/KM KM/vmax

1/vmax 1/[S]

[S]

v 87

Hypothetical

KM = 20

Vmax = 2

88

Enzyme Inhibition Reversible: enzyme activity can be regenerated by removing the inhibitors. Irreversible: complete loss of enzyme activity after a period of time

89

Competitive Inhibition E+S +

k1 k-1

k2 ES  E + P

EI

k3

 KM

E I   K I EI 

I KI

E S   k1  k2 ES  k1

E+Q

k-3

d [ ES ]  k1[ E ][ S ]  k 1[ ES ]  k 2 [ ES ]  0 dt d [ EI ]  k3 [ E ][ I ]  k 3[ EI ]  k 4 [ EI ]  0 dt

Eo  [ E ]  [ ES ]  [ EI ] Eo  [ E ] 

[ E ][ S ] [ E ][ I ]  KM KI

 [S ] [I ]  Eo  [ E ]1    K K M I  

[E] 

Eo [S ] [ I ] 1  KM KI 90

1/v

[I]

d [ P]  k 2 [ ES ] dt

KM  [I ]   1  vmax  K I 

d [ P] [ E ][ S ]  k2 dt KM

1/vmax [S]

d [ P] k 2 Eo [S ]  [ S ] [ I ] dt KM 1  KM KI

v

d [ P]  dt

k 2 Eo [ S ]   [I ] K M 1   [ S ]   KI

vmax  k 2 Eo

1 1 KM   v vmax vmax

vmax [ S ] v  [I ]    [ S ]  K M 1   KI 

 [I ]  1 1    K I  [S ]

Inhibitor is replaced from the active sites by substrate at high [S] 91

Non-competitive inhabitation Inhibitor binds to some other binding sites; Inhibitor combines with both free E and ES 2 possible mechanisms: Ternary complex is a dead-end complex and does not breakdown to yield products Ternary complex breaks down at a slow rate than he ES complex KM ES  E + P +

E+S + I

I

KI EI + S

KM

KI EIS  E + P

92

E+S +

k1 k-1

I

1/v k2 ES  E + P + I

KI EI + S

k3 k-3

KI

 [S ]   K M 1  K M  

EIS  E + P

v  k 2 [ ES ]

1/vmax-app

[S ] v KM  vmax 1  [ S ]  [ I ]  [ I ][ S ] KM K I K IKM

1 vmax  app



1 vmax

[I ]  vmax K I

1/vmax-app

Vmax=k2E0 v vmax

1/(vmaxKI)

Henri-Michaelis-Menton Eq



[S ]  [I ]   [S ]     [ S ]1  K M 1  K K M  I   

1/[S]

1/vmax [I]

93

Uncompetitive inhibition No binding site for inhibitor until substrate is bound to the enzyme, so only ternary complex is possible

94

Uncompetitive Inhibition KM E+S ES  E + P +

1/v

I

KM vmax

KI EIS  E + Q

1

 [I ]  1   vmax  K I 

v  k 2 [ ES ] [S ] v KM  vmax 1  [ S ]  [ I ][ S ] KM K IKM

1/[S]

1 1 [I ]   v' vmax K I 1/v’

Vmax=k2E0

1 1  [ I ]  1 KM 1     v vmax [ S ] vmax  K I 

1/KI 1/vmax [I]

95

E  nS  ES n P K

[ ES n ] [ E ][ S ]n

Yield

Eo  [ E ]  K [ E ][ S ]n [E] 

Hill eq.

[ ES n ] K [ E ][ S ]n Y  [ E ]  [ ES n ] [ E ]  K [ E ][ S ]n

Y  K [ S ]n 1 Y

KEo [ S ]n 1  K [ S ]n

n: Hill coefficient

 Y  log   n log[S ]  log K 1 Y   

v  k 2 [ ES ]

[ ES ] 

Eo 1  K [ S ]n

k 2 E o K [ S ]n v  k 2 [ ES n ]  1  K [ S ]n 1 1 K   n v vmax [ S ] vmax

Eo  [ E ]  [ ES ] 96

97

Chain Reactiosn Chain reactions usually involve free radicals H2+Br2=2HBr The experimental rate law is 1 2

d [ HBr ] k '[ H 2 ][ Br2 ]  [ HBr ] dt 1 k'' [ Br2 ]

98

Initiation



Br2  Br  Br

Propagation

ka



kb Br   H 2  HBr  H 

kc H   Br2  HBr  Br 

Inhibition

Termination

kd H   HBr  H 2 Br 

ke Br   Br   Br2

99

100

101

C2H6 = C2H4 + H2

102

103

The Lindemann Mechanism N2O5 = NO2 + NO3.

k1 >> k-2 [N2O5] Rate  k2[N2O5]2 k1 bAPA

bA PAbB P B R  ks (1  bA PA  bB PB ) 2 bA PAbB P B bB P B ' PB R  ks  ks  ks 2 (bA PA ) bA PA PA

bBPB