(Benjamin, 1.6) David Reckhow CEE 680 #5 1 Elementary Reactions - - PowerPoint PPT Presentation

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(Benjamin, 1.6) David Reckhow CEE 680 #5 1 Elementary Reactions - - PowerPoint PPT Presentation

Print version Updated: 28 January 2020 Lecture #5 Kinetics and Thermodynamics: Fundamentals of Kinetics and Analysis of Kinetic Data (Stumm & Morgan, Chapt.2 ) (pp.16-20; 69-81) (Benjamin, 1.6) David Reckhow CEE 680 #5 1 Elementary


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SLIDE 1

Lecture #5 Kinetics and Thermodynamics: Fundamentals of Kinetics and Analysis of Kinetic Data

(Stumm & Morgan, Chapt.2 ) (pp.16-20; 69-81)

David Reckhow CEE 680 #5 1

(Benjamin, 1.6)

Updated: 28 January 2020

Print version

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SLIDE 2

Elementary Reactions

 When reactant

molecules collide with the right orientation and energy level to form new bonds

 Many “observable”

reactions are really just combinations of elementary reactions

F E B A F C D A E C D C B A + → + + → + → + → + 2 2

David Reckhow CEE 680 #5 2

fast slow fast Starting out with some A and B, we observe that E and F are the end products

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SLIDE 3

Cont.

 Elementary

reactions

 A single step in a

reaction sequence

 Involves 1 or 2 reactants and 1 or 2 products  Can be described by classical chemical

kinetics

David Reckhow CEE 680 #5 3

S&M: Fig. 2.11

  • Pg. 72
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SLIDE 4

Kinetics

 Examples

 Fe+2 oxidation by O2

 almost instantaneous at high pH  quite slow at low pH  high D.O. may help

 Oxidation of organic material  Formation of solid phases

 Aluminum hydroxide  Quartz sand

David Reckhow CEE 680 #5 4

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SLIDE 5

Kinetics

 Base Hydrolysis of dichloromethane (DCM)

 Forms chloromethanol (CM) and chloride  Classic second order reaction (molecularity of 2)

 First order in each reactant, second order overall

David Reckhow CEE 680 #5 5

dt Cl d dt CM d dt OH d dt DCM d OH DCM k Rate ] [ ] [ ] [ ] [ ] ][ [

− − −

= = − = − = =

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SLIDE 6

Reaction Kinetics

 Irreversible reaction

 is one in which the reactant(s) proceed to product(s), but

there is no significant backward reaction,

 In generalized for, irreversible reactions can be represented

as:

aA + bB ⇒ Products

David Reckhow CEE 680 #5 6

i.e., the products do not recombine or change to form reactants in any appreciable amount. An example of an irreversible reaction is hydrogen and oxygen combining to form water in a combustion reaction. We do not observe water spontaneously separating into hydrogen and oxygen.

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SLIDE 7

Reaction Kinetics: Reversibility

 A reversible reaction

 is one in which the reactant(s) proceed to product(s),

but the product(s) react at an appreciable rate to reform reactant(s).

 aA + bB ↔ pP + qQ  Most reactions must be considered reversible

David Reckhow CEE 680 #5 7

An example of a reversible biological reaction is the formation of adenosine triphosphate (ATP) and adenosine diphosphate (ADP). All living organisms use ATP (or a similar compound) to store energy. As the ATP is used it is converted to ADP, the organism then uses food to reconvert the ADP to ATP.

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SLIDE 8

Kinetic principles

 Law of Mass Action

 For elementary reactions

David Reckhow CEE 680 #5 8

where, CA = concentration of reactant species A, [moles/liter] CB = concentration of reactant species B, [moles/liter] a = stoichiometric coefficient of species A b = stoichiometric coefficient of species B k = rate constant, [units are dependent on a and b]

products bB aA

k

→  +

b B a AC

kC rate =

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SLIDE 9

Reaction Kinetics (cont.)

 Reactions of order

“n” in reactant “c”

 When n=0, we have a

simple zero-order reaction

David Reckhow CEE 680 #5 9

dc dt kcn = −

dc dt k = −

kt c c

=

10 20 30 40 50 60 70 80 90 20 40 60 80 Concentration Time (min)

k mg l = 10 / / min

Slope

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SLIDE 10

Reaction Kinetics (cont.)

 When n=1, we

have a simple first-order reaction

 This results in

an “exponential decay”

David Reckhow CEE 680 #5 10

dc dt kc = −

1

c c e

  • kt

=

10 20 30 40 50 60 70 80 90 20 40 60 80 Time (min) Concentration

k =

0 032

1

. min

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SLIDE 11

Reaction Kinetics (cont.)

 This equation can

be linearized

 good for

assessment of “k” from data

David Reckhow CEE 680 #5 11

dc dt kc = −

1 10 100 20 40 60 80 Time (min) Concentration (log scale)

kt c c

= ln ln

k =

0 032

1

. min

Slope

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SLIDE 12

10 20 30 40 50 60 70 80 90 20 40 60 80 Time (min) Concentration

Reaction Kinetics (cont.)

 This results in

an especially wide range in rates

 More typical to

have 2nd order in each of two different reactants

David Reckhow CEE 680 #5 12

dc dt kc = −

2

c c kc t

  • =

+ 1 1

k L mg = 0 0015 . / / min  When n=2, we have a simple second-order reaction

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SLIDE 13

Reaction Kinetics (cont.)

 Again, the equation can be linearized

to estimate “k” from data

David Reckhow CEE 680 #5 13

dc dt kc = −

2

0.02 0.04 0.06 0.08 0.1 0.12 20 40 60 80 Time (min) 1/Concentration

kt c c

  • +

= 1 1

k L mg = 0 0015 . / / min

Slope

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SLIDE 14

Comparison of Reaction Orders

 Curvature as order changes: 2nd>1st>zero

David Reckhow CEE 680 #5 14

10 20 30 40 50 60 70 80 90 20 40 60 80 Time (min) Concentration

Zero Order First Order Second Order

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SLIDE 15

Reaction Kinetics (cont.)

 For most reactions, n=1 for each of two different

reactants, thus a second-order overall reaction

David Reckhow CEE 680 #5 15

1 2 1 1c

kc dt dc − =

1 1 5

min 10 9 . 3

− − −

= Lmg x k

 Many of these will have

  • ne reactant in great

excess

 These become “pseudo- 1st order in the limiting reactant, as the reactant in excess really doesn’t change in concentration

2

c

1

c

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SLIDE 16

10 20 30 40 50 60 70 80 90 20 40 60 80 Time (min) Concentration

Reaction Kinetics (cont.)

 Since C2 changes little

from its initial 820 mg/L, it is more interesting to focus on C1

 C1 exhibits simple 1st

  • rder decay, called

pseudo-1st order

 The pseudo-1st order

rate constant is just the “observed rate” or kobs

David Reckhow CEE 680 #5 16

1 2 1 1c

kc dt dc − =

t k

  • bs

e c c

=

1 1

1 5 2

min 032 . ) 820 ( 10 9 . 3

− −

≈ = ≈ x kc kobs

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SLIDE 17

Variable Kinetic Order

 Any reaction order, except n=1

David Reckhow CEE 680 #5 17

n

kc dt dc − =

( )

[ ] (

)

1 1 1

1 1 1

− −

− + =

n n

  • t

kc n c c

( )kt

n c c

n

  • n

1 1 1

1 1

− + =

− −

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SLIDE 18

Half-lives

 Time required for initial concentration to drop to

half, i.e.., c=0.5co

 For a zero order reaction:  For a first order reaction:

David Reckhow CEE 680 #5 18

c c kt

  • =

2 1

5 . kt c c

= k c t

  • 5

.

2 1 =

c c e

  • kt

=

2 1

5 .

kt

  • e

c c

=

k k t 693 . ) 2 ln(

2 1

= =

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SLIDE 19

Kinetic problem

 If the half-life of bromide in the presence of excess

chlorine is 13 seconds (pseudo-1st order reaction,

 What is the pseudo-1st order rate constant  how long does it take for 99% of the bromide to be

  • xidized?

David Reckhow CEE 680 #5 19

HOCl Br HOBr Cl

k

+  →  +

− −

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SLIDE 20

Reactions in Series

David Reckhow CEE 680 #5 20

D C B A

k k k

→  →  → 

3 2 1

  • Fig. 2.9
  • Pg. 68

k1=k2=k3=0.1 day-1

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SLIDE 21

Reversible reaction kinetics

David Reckhow CEE 680 #5 21

For a general reversible reaction:

f b

k aA + bB pP + qQ k ↔

And the rate law must consider both forward and reverse reactions:

A f A a B b b P p Q q

r = k C C - k C C

where, kf = forward rate constant, [units depend on a and b] kb = backward rate constant, [units depend on a and b] CP = concentration of product species P, [moles/liter] CQ = concentration of product species Q, [moles/liter] p = stoichiometric coefficient of species P q = stoichiometric coefficient of species Q

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SLIDE 22

Reversible 1st order reactions

 Kinetic law  Eventually the

reaction slows and,

 Reactant

concentrations approach the equilibrium values

David Reckhow CEE 680 #5 22

  • Fig. 2.10
  • Pg. 69

] [ ] [

2 1

B k A k dt dB − =

eq

K k k A B B k A k dt dB ≡ = − = =

2 1 2 1

] [ ] [ ] [ ] [

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SLIDE 23

Analysis of Rate Data

 Integral Method

 Least squares regression of linearized form

 Differential Method

 estimate instantaneous rate at known time and

reactant concentration

 Initial rate Method

 more rigorous, but slow

 Method of Excess

 only when 2 or more reactants are involved

David Reckhow CEE 680 #5 23

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SLIDE 24

Kinetic model for equilibrium

D C B A D C B A

b f

k k

+  ← + + →  +

} }{ { B A k r

f f =

David Reckhow CEE 680 #5 24

 Consider a reaction as

follows:

 Since all reactions are

reversible, we have two possibilities

 The rates are:  And at equilibrium the two

are equal, rf=rb

 We then define an

equilibrium constant (Keq)

} }{ { D C k r

b b =

A + B = C + D

} }{ { } }{ { B A D C k k K

b f eq

= ≡

} }{ { } }{ { D C k B A k

b f

=

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SLIDE 25

Kinetic model with moles

[ ] [ ] B

A f f

B A k r γ γ =

David Reckhow CEE 680 #5 25

 In terms of molar concentrations, the rates are:  And at equilibrium the two are equal, rf=rb  And solving for the equilibrium constant (Keq)

[ ] [ ] D

C b b

D C k r γ γ =

[ ] [ ] [ ] [ ] [ ][ ] [ ][ ]

        = = ≡

B A D C B A D C b f eq

B A D C B A D C k k K γ γ γ γ γ γ γ γ

[ ] [ ] [ ] [ ] D

C b B A f

D C k B A k γ γ γ γ =

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SLIDE 26

To next lecture

David Reckhow CEE 680 #5 26