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Reaction Rates / Kinetics
• Chemical rxn, reactant consumed,product formed
• Amt reactant decrease ↓, Amt product increase ↑
• Rate follow stoichiometric principles
A → B
• For every ONE A breakdown = ONE B will form
• Rate decomposition A= Rate formation of B
dt
Bd
dt
Ad ][][ 


2NO2 → N2O4
• Two mole NO2 decompose = One mole N2O4 form
• NO2 used up is twice as fast as N2O4 produced
dt
ONd
dt
NOd ][1
2
][1 422 


dt
HId
dt
Id
dt
Hd
2
][][1][1 22 




H2 + I2 → 2HI
• One mole H2 decompose = TWO mole HI form
• Rate H2 and I2 decompositionthe same
but only half the rate HI formation
Amt/Conc Amt/Conc
Time Time
Reactants Product
(Reactants)
• X decrease/consume ↓ over time
(Products)
• Y increase/form ↑over time
Rate of Decrease of X
• Decrease ↓ Conc X /time
• Decrease ↓ Vol X /Time
• Decrease ↓ Abs X /Time
Rate of Increase of Y
• Increase ↑ Conc Y /time
• Increase ↑ Vol Y /Time
• Increase ↑ Abs Y /Time
Amt/Conc/Vol/Abs X
Time
Amt/Conc/Vol/Abs Y
X
Y
Time
Gradient= rate change at time,t Gradient= rate change at time,t
Instantaneous rate
time, t1
Initial rate, t = 0
Initial rate, t = 0
Instantaneous rate
time, t1
X → Y
Click here notes
GraphicalRepresentationof Order :ZERO, FIRST and SECOND order
ZERO ORDER FIRST ORDER SECOND ORDER
Rate – 2nd order respect to [A]
Conc x2 – Rate x 4
Unit for k
Rate = k[A]2
Rate = kA2
k = M-1s-1
Rate
Conc reactant
Rate
Conc reactant Conc reactant
Conc Conc Conc
Time Time Time
Time
Conc reactant
Rate
Time
ln At
Time
1/At
ktAA ot  ][][
Rate = k[A]0
Rate independent of [A]
Unit for k
Rate = k[A]0
Rate = k
k = Ms-1
Rate vs Conc – Constant
Conc vs Time – Linear
Rate = k[A]1
Rate - 1st order respect to [A]
Unit for k
Rate = k[A]1
Rate = kA
k = s-1
Rate vs Conc - proportional
Conc vs Time
ktAA
eAA
ot
kt
ot

 
]ln[]ln[
][][
[A]t
[A]o
kt
AA ot

][
1
][
1
ln Ao
1/Ao
Conc at time t Conc at time t
Order of rxn found using THREE mtds
Initial Rate mtd
(Multiple Single Runs)
Conc Vs Time Mtd
(Half Life)
Conc Vs Time Mtd
(Whole Curve/Tangent)
Multiple Single Runs
Vary/Keep certain conc fixed
Wasteful as multiple runs needed
Monitor decrease in conc reactant
Using Half Life to determine order
Monitor decrease conc of single reactant
Using gradient/ tangent at diff conc
Conc x2 – rate x2 - 1st order
Conc x2 – rate x4 – 2nd order
Conc x2 – rate 0 – zero order Convert Conc Vs Time to Rate vs Conc
Rate Vs Conc – Linear – 1st Order
Initial Rate taken, time 0
Draw tangent at time 0
Half Life directly prop to Conc
Half Life inversely prop to Conc
Expt Conc
A
Conc
B
Initial rate
1 0.01 0.02 2
2 0.01 0.04 4
3 0.02 0.02 4
Conc
Time
Expt 2
Expt 1
Conc reactant
Time
Zero order
Conc reactant
Time
Half Life constant
1st order
2nd order
Conc reactant
Time
Gradient at diff conc
Conc
Rate
A + B → AB
Find order A (fix conc B )
Let Rate = k[A]x[B] y
Rate = k[A]2 [B]1
2nd order respect to A 1st order respect to B
Using Initial rate for order of rxn
Find order B (fix conc A)
Let Rate = k[A]x[B] y
2
806.0log652.0lg
806.0652.0
0713.0
0575.0
1026.1
1021.8
2.
1.
2.
1.
2
3





















x
x
Conc
Conc
Rate
Rate
x
x
x
1
649.0log652.0lg
649.0652.0
0333.0
0216.0
1026.1
1021.8
3.
1.
3.
1.
2
3





















y
y
Conc
Conc
Rate
Rate
y
y
y
Expt Conc
A
Conc
B
Initial rate
1 0.0575 0.0216 8.21 x 10-3
2 0.0713 0.0216 1.26 x 10-2
3 0.0575 0.0333 1.26 x 10-2
Expt Conc
F2
Conc
CIO2
Initial rate
1 0.10 0.01 1.2 x 10-3
2 0.10 0.04 4.8 x 10-3
3 0.20 0.01 2.4 x 10-3
F2 + 2CIO2 → 2FCIO2
Find order CIO2 (fix conc F2 )
Let Rate = k[F2]x [CIO2] y
Find order F2 (fix conc CIO2)
Let Rate = k[F2]x [CIO2] y
1st order respect to CIO2 1st order respect to F2
Rate = k [CIO2]1
[F2]1
1
44
01.0
04.0
102.1
108.4
1.
2.
1.
2.
3
3




















y
Conc
Conc
Rate
Rate
y
y
y
1
22
10.0
20.0
102.1
104.2
1.
3.
1.
3.
3
3




















x
Conc
Conc
Rate
Rate
x
x
x
To calculate k
Expt 1 : Ini rate = 1.2 x 10-3, [F2] = 0.10M, [CIO2] = 0.01M
Rate = k[F2]1[CIO2]1
1.2 x 10-3 = k[0.10]1[0.01]1, k = 1.2 M-1s-1
To calculate k
Expt 1 : Ini rate = 8.21 x 10-3, [A] = 0.0575, [B] = 0.0216
Rate = k[A]2[B]1
8.21 x 10-3 = k[0.0575]2[0.0216]1, k = 115
2CIO2 + 2OH-
→ CIO3
-
+ CIO2
-
+ H2O
Find order CIO2 (fix conc OH-
)
Let Rate = k[CIO2]x[OH-
]y
Expt 1 : Ini rate = 8 x 10-3 , [CIO2] = 0.025M, [OH-
] = 0.046M
Rate = k[CIO2]2[OH-
] 1
8 x 10-3 = k[0.025]1[0.046]1, k = 278.3M-1s-1
Find order OH-
(fix conc CIO2 )
Let Rate = k[CIO2]x[OH-
]y
2nd order respect to CIO2
1st order respect to OH-
Rate = k[CIO2]2[OH-
]1
Using Initial rate for order of rxn
To calculatek
2
4.1log96.1lg
4.196.1
025.0
035.0
1000.8
1057.1
1.
2.
1.
2.
3
2





















x
x
Conc
Conc
Rate
Rate
x
x
x
1
22
046.0
092.0
1057.1
1014.3
2.
3.
2.
3.
2
2




















y
Conc
Conc
Rate
Rate
y
y
y
Expt Conc
OH
Conc
CIO2
Initial rate
1 0.046 0.025 8 x 10-3
2 0.046 0.035 1.57 x 10-3
3 0.096 0.035 3.14 x 10-3
Br2 + 2NO → 2NOBr
Find order Br2 (fix conc NO )
Let Rate = k[Br2]x[NO]y
Find order NO (fix conc Br2 )
Let Rate = k[Br2]x[NO]y
Expt Conc
Br2
Conc
NO
Initial rate
1 0.1 0.1 12
2 0.2 0.1 24
3 0.1 0.2 48
1
2
1
2
1
2.0
1.0
24
12
2.
1.
2.
1.






















x
Conc
Conc
Rate
Rate
x
x
x
2
2
1
4
1
2.0
1.0
48
12
3.
1.
3.
1.






















y
Conc
Conc
Rate
Rate
y
y
y
2nd order respect to NO1st order respect to Br2
Rate = k[Br2]1[NO]2
Expt 1 : Ini rate = 12Ms-1, [Br2] = 0.1M, [NO] = 0.1M
Rate = k[Br2]1[NO]2
12 = k[0.1]1[0.1]2 , k = 12,000 M-1min-1
To calculatek
Conc Vs Time / Conc Vs Rate for Order
2A → B + C
Plot Conc A vs Time for order, initial rate and rate constant, k
2N205 → 4N02 + 02
Plot Rate vs Conc for order and rate constant, k
Conc vs Time Mtd
• Half Life A -constant =80s
• 1st orderrespect to [A]
• Formulafor 1st order half life
Conc vs Rate Mtd
• Straight Line – 1st order respect to [N205]
• Rate = k[N205 ], k = gradient = 7.86 x 10-6 s-1
Time 0 40 80 120 160 200 240
Conc 0.8 0.58 0.40 0.28 0.20 0.14 0.10
Conc
Time
80s 80s 80s
13
2/1
1066.8
80
693.0
693.0



sk
k
t
Conc Rate
/10-5
0.94 1.26
1.40 1.52
1.79 1.93
2.00 2.10
2.21 2.26
Conc
Rate
rate constant
Rate Law / Rate Expression
Rxn: aA + bB → cC + dD
• Stoichiometry eqn : Show mole ratio of reactant/product
• Rate eqn : Eqn relate rate with conc of reactant
: How conc reactant affect rate
Rxn eqn = k[A]x[B]y x = order respect to [A]
y = order respect to [B]
(x +y) = overall order
k = rate constant
Order must be determined experimentally , NOT derived from stoichiometry coefficients
Gradient = k
Using Initial rate and Half Life for order
Hydrolysis of ester by OH-
: Ester + OH- → X + Y
Rxn done using two diff OH- conc.
Run 1 – [OH- ] – 0.20M Run 2 – [OH-] – 0.40M
Plot Conc ester vs Time. Find order and initial rate
Find order for OH- (fix conc ester)
Let Rate = k[OH-]x [ester] y
Find order for ester (UsingHalf Life )
Using expt 2 : Conc ester vs time
Half Life Ester t1/2 = 12 m(constant)
1st order respect to ester
Rate = k[OH-]1 [ester]1
For EXPT 2 :
• Ini rate = 8.00, [OH-]= 0.4M, [ester] = 100M
• Rate = k[OH-]1 [ester]1
• 8.00 = k[0.4]1[100]1
• k = 0.2M-1min-1
Half life : 100 → 50→ 25 (12 min)
• Ini Rate expt 1 – Gradient time 0 = 4.00
• Ini Rate expt 2 – Gradient time 0 = 8.00
1st order respect to OH -
Conc ester
Time
Expt 2- [OH] = 0.40M
Expt 1 - [OH] = 0.20M
Compare Expt 1 and 2
1
2
1
2
1
40.0
20.0
00.8
00.4
2.
1.
2.
1.






















x
Conc
Conc
Rate
Rate
x
x
x
Conc ester
Time
Expt 1 - [OH] = 0.20M
Expt 2- [OH] = 0.40M
Gradient, rate = 4.00
Gradient, rate = 8.00
12 m 12 m
RBr + OH- → ROH + Br-
Rxn done using TWO diff conc OH-
Expt 1 – [OH- ] – 0.10M Run 2 – [OH- ] – 0.15M
Plot Conc RBr vs time. Find order and initial rate
Determine order for OH- (fix conc RBr)
Let Rate = k[OH-]x [RBr] y
Find order RBr (using half life)
Using expt 2 : Conc vs time
Half Life RBr t1/2 = 78 m
Rate = k[OH-]1 [RBr]1
• For expt 1
Ini rate = 5.25, [OH-] = 0.10M, [RBr] = 0.01M
• Rate = k[OH-]1 [RBr]1
• 5.25 = k[0.10]1[0.01]1
• k = 5250 M-1min-1
Half life: 0.01 → 0.005 → 0.0025 = 78 m
Ini Rate expt 1 – Gradient time 0 = 5.25
Ini Rate expt 2 – Gradient time 0 = 8.00
1st order with respect to OH -
Rate = k[OH-]1 [RBr]1
Using Initial rate and Half Life for order
1
65.065.0
15.0
10.0
00.8
25.5
2.
1.
2.
1.
















x
Conc
Conc
Rate
Rate
x
x
x
Expt 1 Expt 2
Time/m [RBr]/M
in [OH] = 0.10
[RBr]/M
in [OH] = 0.15
0 0.0100 0.0100
40 0.0079 0.0070
80 0.0062 0.0049
120 0.0049 0.0034
160 0.0038 0.0024
200 0.0030 0.0017
240 0.0024 0.0012
Expt 1 - [OH] = 0.20M
Expt 2- [OH] = 0.15M
Time
Conc
RBr
78s 78s
Gradient, rate = 8.00
Gradient, rate = 5.25
1st order with respect to RBr
Ester + H2O → CH3CO2H + C2H5OH
Rxn done using TWO diff HCI conc
Expt 1 : [HCI] – 0.10M Expt 2 :[HCI] – 0.20M
Plot Conc Estervs time. Find order and rate of rxn
Find order HCI (fix conc Ester)
Rate = k[HCI]1[Ester]1
1st order respect to HCI
Using Initial rate and Half Life for order
Expt 1 Expt 2
Time/m [Ester]/M
in [HCI] = 0.1
[Ester]/M
in [HCI] = 0.2
0 0.200 0.200
25 0.152 0.115
50 0.115 0.067
75 0.088 0.038
100 0.067 0.022
120 0.051 0.013
Time
Conc
Ester
Gradient, rate = 1.9
Conc
Ester
Time
Gradient, rate = 3.8
Find order Ester (use half life)
Half life Ester -> 0.200 → 0.100 → 0.050 = 31 m
31 m 31 m
1st order respect to Ester
1
5.05.0
2.0
1.0
8.3
9.1
2.
1.
2.
1.
















x
Conc
Conc
Rate
Rate
x
x
x
Ini rate Expt 1 – Gradient time 0 = 1.90
Ini rate Expt 2 – Gradient time 0 = 3.80
Expt 1 Expt 2
Half life is 31 min (constant)
Ini rate Expt 1 – Gradient time 0 = 1.90
Ini rate Expt 2 – Gradient time 0 = 3.80
C3H8 + 5O2 → 3CO2 + 4H2O2H2 + O2 → 2H2O
Rate O2 decrease ↓ is 0.23Ms-1
,
what is rate of H2O formation/increases↑
Rate C3H8 decrease ↓ is 0.30Ms-1
,
what is the rate of 02 decrease ↓
Rxn Rates / Kinetics
122
22
2
46.0)23.0(2
][
2
][
2
][1
1
][1
2
][
1
][1
2
][1 22




Ms
dt
Od
dt
OHd
dt
OHd
dt
Od
dt
OHd
dt
Od
dt
Hd
1832
832
283
5.1)30.0(5
][
5
][
1
][1
5
][1
3
][1
5
][1
1
][1 2




Ms
dt
HCd
dt
Od
dt
HCd
dt
Od
dt
COd
dt
Od
dt
HCd
Benzenediazonium chloride, unstable, decomposes to produce N2 gas shown below
C6H5N2
+CI- + H2O → C6H5OH + N2 + HCI
Vol of N2 was collected over time
Vol of gas produced N2 in time t is proportional to amt C6H5N2
+CI- used up
V∞ α [C6H5N2
+CI- ] at start
(V∞ - Vt ) α [C6H5N2
+CI- ] remaining at time t
Plot of (V∞ - Vt ) vs time = Plot of conc vs time
Time/t 0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 ∞
Vt = Vol N2 0 14 28 41 54 65 76 87 96 104 112 120 127 133 139 219
(V∞ – Vt)/
cm3
219 205 191 178 165 154 143 132 123 115 107 99 92 86 139 0
Find rate at
diff conc
Time
Plot of (V∞ - Vt ) vs time = Conc vs time(V∞ - Vt )
Time Conc
V∞ - Vt
Rate/
Slope
0 219 16.5
4 165 12.1
7 132 10.0
14 80 6.22
21 47 3.84
(V∞ - Vt )
Rate
Plot Rate vs Concslope = rate

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IB Chemistry Order Reaction, Rate Law and Half life

  • 1. Reaction Rates / Kinetics • Chemical rxn, reactant consumed,product formed • Amt reactant decrease ↓, Amt product increase ↑ • Rate follow stoichiometric principles A → B • For every ONE A breakdown = ONE B will form • Rate decomposition A= Rate formation of B dt Bd dt Ad ][][    2NO2 → N2O4 • Two mole NO2 decompose = One mole N2O4 form • NO2 used up is twice as fast as N2O4 produced dt ONd dt NOd ][1 2 ][1 422    dt HId dt Id dt Hd 2 ][][1][1 22      H2 + I2 → 2HI • One mole H2 decompose = TWO mole HI form • Rate H2 and I2 decompositionthe same but only half the rate HI formation Amt/Conc Amt/Conc Time Time Reactants Product (Reactants) • X decrease/consume ↓ over time (Products) • Y increase/form ↑over time Rate of Decrease of X • Decrease ↓ Conc X /time • Decrease ↓ Vol X /Time • Decrease ↓ Abs X /Time Rate of Increase of Y • Increase ↑ Conc Y /time • Increase ↑ Vol Y /Time • Increase ↑ Abs Y /Time Amt/Conc/Vol/Abs X Time Amt/Conc/Vol/Abs Y X Y Time Gradient= rate change at time,t Gradient= rate change at time,t Instantaneous rate time, t1 Initial rate, t = 0 Initial rate, t = 0 Instantaneous rate time, t1 X → Y Click here notes
  • 2. GraphicalRepresentationof Order :ZERO, FIRST and SECOND order ZERO ORDER FIRST ORDER SECOND ORDER Rate – 2nd order respect to [A] Conc x2 – Rate x 4 Unit for k Rate = k[A]2 Rate = kA2 k = M-1s-1 Rate Conc reactant Rate Conc reactant Conc reactant Conc Conc Conc Time Time Time Time Conc reactant Rate Time ln At Time 1/At ktAA ot  ][][ Rate = k[A]0 Rate independent of [A] Unit for k Rate = k[A]0 Rate = k k = Ms-1 Rate vs Conc – Constant Conc vs Time – Linear Rate = k[A]1 Rate - 1st order respect to [A] Unit for k Rate = k[A]1 Rate = kA k = s-1 Rate vs Conc - proportional Conc vs Time ktAA eAA ot kt ot    ]ln[]ln[ ][][ [A]t [A]o kt AA ot  ][ 1 ][ 1 ln Ao 1/Ao Conc at time t Conc at time t
  • 3. Order of rxn found using THREE mtds Initial Rate mtd (Multiple Single Runs) Conc Vs Time Mtd (Half Life) Conc Vs Time Mtd (Whole Curve/Tangent) Multiple Single Runs Vary/Keep certain conc fixed Wasteful as multiple runs needed Monitor decrease in conc reactant Using Half Life to determine order Monitor decrease conc of single reactant Using gradient/ tangent at diff conc Conc x2 – rate x2 - 1st order Conc x2 – rate x4 – 2nd order Conc x2 – rate 0 – zero order Convert Conc Vs Time to Rate vs Conc Rate Vs Conc – Linear – 1st Order Initial Rate taken, time 0 Draw tangent at time 0 Half Life directly prop to Conc Half Life inversely prop to Conc Expt Conc A Conc B Initial rate 1 0.01 0.02 2 2 0.01 0.04 4 3 0.02 0.02 4 Conc Time Expt 2 Expt 1 Conc reactant Time Zero order Conc reactant Time Half Life constant 1st order 2nd order Conc reactant Time Gradient at diff conc Conc Rate
  • 4. A + B → AB Find order A (fix conc B ) Let Rate = k[A]x[B] y Rate = k[A]2 [B]1 2nd order respect to A 1st order respect to B Using Initial rate for order of rxn Find order B (fix conc A) Let Rate = k[A]x[B] y 2 806.0log652.0lg 806.0652.0 0713.0 0575.0 1026.1 1021.8 2. 1. 2. 1. 2 3                      x x Conc Conc Rate Rate x x x 1 649.0log652.0lg 649.0652.0 0333.0 0216.0 1026.1 1021.8 3. 1. 3. 1. 2 3                      y y Conc Conc Rate Rate y y y Expt Conc A Conc B Initial rate 1 0.0575 0.0216 8.21 x 10-3 2 0.0713 0.0216 1.26 x 10-2 3 0.0575 0.0333 1.26 x 10-2 Expt Conc F2 Conc CIO2 Initial rate 1 0.10 0.01 1.2 x 10-3 2 0.10 0.04 4.8 x 10-3 3 0.20 0.01 2.4 x 10-3 F2 + 2CIO2 → 2FCIO2 Find order CIO2 (fix conc F2 ) Let Rate = k[F2]x [CIO2] y Find order F2 (fix conc CIO2) Let Rate = k[F2]x [CIO2] y 1st order respect to CIO2 1st order respect to F2 Rate = k [CIO2]1 [F2]1 1 44 01.0 04.0 102.1 108.4 1. 2. 1. 2. 3 3                     y Conc Conc Rate Rate y y y 1 22 10.0 20.0 102.1 104.2 1. 3. 1. 3. 3 3                     x Conc Conc Rate Rate x x x To calculate k Expt 1 : Ini rate = 1.2 x 10-3, [F2] = 0.10M, [CIO2] = 0.01M Rate = k[F2]1[CIO2]1 1.2 x 10-3 = k[0.10]1[0.01]1, k = 1.2 M-1s-1 To calculate k Expt 1 : Ini rate = 8.21 x 10-3, [A] = 0.0575, [B] = 0.0216 Rate = k[A]2[B]1 8.21 x 10-3 = k[0.0575]2[0.0216]1, k = 115
  • 5. 2CIO2 + 2OH- → CIO3 - + CIO2 - + H2O Find order CIO2 (fix conc OH- ) Let Rate = k[CIO2]x[OH- ]y Expt 1 : Ini rate = 8 x 10-3 , [CIO2] = 0.025M, [OH- ] = 0.046M Rate = k[CIO2]2[OH- ] 1 8 x 10-3 = k[0.025]1[0.046]1, k = 278.3M-1s-1 Find order OH- (fix conc CIO2 ) Let Rate = k[CIO2]x[OH- ]y 2nd order respect to CIO2 1st order respect to OH- Rate = k[CIO2]2[OH- ]1 Using Initial rate for order of rxn To calculatek 2 4.1log96.1lg 4.196.1 025.0 035.0 1000.8 1057.1 1. 2. 1. 2. 3 2                      x x Conc Conc Rate Rate x x x 1 22 046.0 092.0 1057.1 1014.3 2. 3. 2. 3. 2 2                     y Conc Conc Rate Rate y y y Expt Conc OH Conc CIO2 Initial rate 1 0.046 0.025 8 x 10-3 2 0.046 0.035 1.57 x 10-3 3 0.096 0.035 3.14 x 10-3 Br2 + 2NO → 2NOBr Find order Br2 (fix conc NO ) Let Rate = k[Br2]x[NO]y Find order NO (fix conc Br2 ) Let Rate = k[Br2]x[NO]y Expt Conc Br2 Conc NO Initial rate 1 0.1 0.1 12 2 0.2 0.1 24 3 0.1 0.2 48 1 2 1 2 1 2.0 1.0 24 12 2. 1. 2. 1.                       x Conc Conc Rate Rate x x x 2 2 1 4 1 2.0 1.0 48 12 3. 1. 3. 1.                       y Conc Conc Rate Rate y y y 2nd order respect to NO1st order respect to Br2 Rate = k[Br2]1[NO]2 Expt 1 : Ini rate = 12Ms-1, [Br2] = 0.1M, [NO] = 0.1M Rate = k[Br2]1[NO]2 12 = k[0.1]1[0.1]2 , k = 12,000 M-1min-1 To calculatek
  • 6. Conc Vs Time / Conc Vs Rate for Order 2A → B + C Plot Conc A vs Time for order, initial rate and rate constant, k 2N205 → 4N02 + 02 Plot Rate vs Conc for order and rate constant, k Conc vs Time Mtd • Half Life A -constant =80s • 1st orderrespect to [A] • Formulafor 1st order half life Conc vs Rate Mtd • Straight Line – 1st order respect to [N205] • Rate = k[N205 ], k = gradient = 7.86 x 10-6 s-1 Time 0 40 80 120 160 200 240 Conc 0.8 0.58 0.40 0.28 0.20 0.14 0.10 Conc Time 80s 80s 80s 13 2/1 1066.8 80 693.0 693.0    sk k t Conc Rate /10-5 0.94 1.26 1.40 1.52 1.79 1.93 2.00 2.10 2.21 2.26 Conc Rate rate constant Rate Law / Rate Expression Rxn: aA + bB → cC + dD • Stoichiometry eqn : Show mole ratio of reactant/product • Rate eqn : Eqn relate rate with conc of reactant : How conc reactant affect rate Rxn eqn = k[A]x[B]y x = order respect to [A] y = order respect to [B] (x +y) = overall order k = rate constant Order must be determined experimentally , NOT derived from stoichiometry coefficients Gradient = k
  • 7. Using Initial rate and Half Life for order Hydrolysis of ester by OH- : Ester + OH- → X + Y Rxn done using two diff OH- conc. Run 1 – [OH- ] – 0.20M Run 2 – [OH-] – 0.40M Plot Conc ester vs Time. Find order and initial rate Find order for OH- (fix conc ester) Let Rate = k[OH-]x [ester] y Find order for ester (UsingHalf Life ) Using expt 2 : Conc ester vs time Half Life Ester t1/2 = 12 m(constant) 1st order respect to ester Rate = k[OH-]1 [ester]1 For EXPT 2 : • Ini rate = 8.00, [OH-]= 0.4M, [ester] = 100M • Rate = k[OH-]1 [ester]1 • 8.00 = k[0.4]1[100]1 • k = 0.2M-1min-1 Half life : 100 → 50→ 25 (12 min) • Ini Rate expt 1 – Gradient time 0 = 4.00 • Ini Rate expt 2 – Gradient time 0 = 8.00 1st order respect to OH - Conc ester Time Expt 2- [OH] = 0.40M Expt 1 - [OH] = 0.20M Compare Expt 1 and 2 1 2 1 2 1 40.0 20.0 00.8 00.4 2. 1. 2. 1.                       x Conc Conc Rate Rate x x x Conc ester Time Expt 1 - [OH] = 0.20M Expt 2- [OH] = 0.40M Gradient, rate = 4.00 Gradient, rate = 8.00 12 m 12 m
  • 8. RBr + OH- → ROH + Br- Rxn done using TWO diff conc OH- Expt 1 – [OH- ] – 0.10M Run 2 – [OH- ] – 0.15M Plot Conc RBr vs time. Find order and initial rate Determine order for OH- (fix conc RBr) Let Rate = k[OH-]x [RBr] y Find order RBr (using half life) Using expt 2 : Conc vs time Half Life RBr t1/2 = 78 m Rate = k[OH-]1 [RBr]1 • For expt 1 Ini rate = 5.25, [OH-] = 0.10M, [RBr] = 0.01M • Rate = k[OH-]1 [RBr]1 • 5.25 = k[0.10]1[0.01]1 • k = 5250 M-1min-1 Half life: 0.01 → 0.005 → 0.0025 = 78 m Ini Rate expt 1 – Gradient time 0 = 5.25 Ini Rate expt 2 – Gradient time 0 = 8.00 1st order with respect to OH - Rate = k[OH-]1 [RBr]1 Using Initial rate and Half Life for order 1 65.065.0 15.0 10.0 00.8 25.5 2. 1. 2. 1.                 x Conc Conc Rate Rate x x x Expt 1 Expt 2 Time/m [RBr]/M in [OH] = 0.10 [RBr]/M in [OH] = 0.15 0 0.0100 0.0100 40 0.0079 0.0070 80 0.0062 0.0049 120 0.0049 0.0034 160 0.0038 0.0024 200 0.0030 0.0017 240 0.0024 0.0012 Expt 1 - [OH] = 0.20M Expt 2- [OH] = 0.15M Time Conc RBr 78s 78s Gradient, rate = 8.00 Gradient, rate = 5.25 1st order with respect to RBr
  • 9. Ester + H2O → CH3CO2H + C2H5OH Rxn done using TWO diff HCI conc Expt 1 : [HCI] – 0.10M Expt 2 :[HCI] – 0.20M Plot Conc Estervs time. Find order and rate of rxn Find order HCI (fix conc Ester) Rate = k[HCI]1[Ester]1 1st order respect to HCI Using Initial rate and Half Life for order Expt 1 Expt 2 Time/m [Ester]/M in [HCI] = 0.1 [Ester]/M in [HCI] = 0.2 0 0.200 0.200 25 0.152 0.115 50 0.115 0.067 75 0.088 0.038 100 0.067 0.022 120 0.051 0.013 Time Conc Ester Gradient, rate = 1.9 Conc Ester Time Gradient, rate = 3.8 Find order Ester (use half life) Half life Ester -> 0.200 → 0.100 → 0.050 = 31 m 31 m 31 m 1st order respect to Ester 1 5.05.0 2.0 1.0 8.3 9.1 2. 1. 2. 1.                 x Conc Conc Rate Rate x x x Ini rate Expt 1 – Gradient time 0 = 1.90 Ini rate Expt 2 – Gradient time 0 = 3.80 Expt 1 Expt 2 Half life is 31 min (constant) Ini rate Expt 1 – Gradient time 0 = 1.90 Ini rate Expt 2 – Gradient time 0 = 3.80
  • 10. C3H8 + 5O2 → 3CO2 + 4H2O2H2 + O2 → 2H2O Rate O2 decrease ↓ is 0.23Ms-1 , what is rate of H2O formation/increases↑ Rate C3H8 decrease ↓ is 0.30Ms-1 , what is the rate of 02 decrease ↓ Rxn Rates / Kinetics 122 22 2 46.0)23.0(2 ][ 2 ][ 2 ][1 1 ][1 2 ][ 1 ][1 2 ][1 22     Ms dt Od dt OHd dt OHd dt Od dt OHd dt Od dt Hd 1832 832 283 5.1)30.0(5 ][ 5 ][ 1 ][1 5 ][1 3 ][1 5 ][1 1 ][1 2     Ms dt HCd dt Od dt HCd dt Od dt COd dt Od dt HCd Benzenediazonium chloride, unstable, decomposes to produce N2 gas shown below C6H5N2 +CI- + H2O → C6H5OH + N2 + HCI Vol of N2 was collected over time Vol of gas produced N2 in time t is proportional to amt C6H5N2 +CI- used up V∞ α [C6H5N2 +CI- ] at start (V∞ - Vt ) α [C6H5N2 +CI- ] remaining at time t Plot of (V∞ - Vt ) vs time = Plot of conc vs time Time/t 0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 ∞ Vt = Vol N2 0 14 28 41 54 65 76 87 96 104 112 120 127 133 139 219 (V∞ – Vt)/ cm3 219 205 191 178 165 154 143 132 123 115 107 99 92 86 139 0 Find rate at diff conc Time Plot of (V∞ - Vt ) vs time = Conc vs time(V∞ - Vt ) Time Conc V∞ - Vt Rate/ Slope 0 219 16.5 4 165 12.1 7 132 10.0 14 80 6.22 21 47 3.84 (V∞ - Vt ) Rate Plot Rate vs Concslope = rate