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8/4/2019 Expt 6 - Chemical Kinetics
http://slidepdf.com/reader/full/expt-6-chemical-kinetics 1/5
MAPUA INSTITUTE OF TECHNOLOGY
School of Chemical Engineering, Chemistry, Biological Engineering, and Material Science and Engineering
Physical Chemistry Laboratory 2 - 3rd
Quarter SY 2010-2011
Neil Patrick P. Tangara , 3rd
Year B.S. Chemical Engineering
Experiment 6 │ Group 5 │ March 1, 2011 1 of 5
Experiment No. 6
CHEMICAL KINETICS: THE HYDROLYSIS OF METHYL ACETATE
Meynard Austria1
, Neil Patrick Tangara, Darlene Pudolin, Emily Rose Santos, Aeiocellis Tan, Creza Loraine Talingting2
1Professor;
2Students, all from CHM171L/A31, School of Chemical Engineering, Chemistry, Biological Engineering & Material Science
and Engineering, Mapua Institute of Technology
ABSTRACT
This experiment intends to determine the order of reaction, rate law constant, and activation energy needed to
initiate the reaction. Also, the effects of temperature, concentration, catalyst, and other parameters such as
pressure on the rate of reaction have been investigated using chemical kinetics. The hydrolysis of Methyl
Acetate was carried out with HCl as the catalyst. It was found to be a 2nd order reaction with respect to the acid
and had an activation energy value of 375,254.0016 J/mole. It was found that increasing both the temperature
and the amount of catalyst present hasten the rate of reaction by an appreciable value by providing it moreenergy and an optimal reaction condition, respectively. Chemistry theories such as the kinetic molecular and
collision theories have been taken into consideration upon interpretation of the results gathered. This report
will discuss why such a phenomenon occurs.
Keywords: rate law constant, order of reaction, activation energy, catalyst
INTRODUCTION
Chemical kinetics is the study and
discussion of chemical reactions with respect toreaction rates, effect of various variables, re-
arrangement of atoms, formation of intermediates
etc.
At the macroscopic level, we are interested in
amounts reacted, formed, and the rates of their
formation. At the molecular or microscopic level,
the following considerations must also be made in
the discusion of chemical reaction mechanism.
Molecules or atoms of reactants must collide with
each other in chemical reactions.
The molecules must have sufficient energy
(discussed in terms of activation energy) to initiate
the reaction.
In some cases, the orientation of the molecules
during the collision must also be considered.
Methyl acetate hydrolyzes to form acetic acid
and methanol, according to the following reaction:
(1)
The reaction is extremely slow in pure
water, but is catalyzed by both hydronium and
hydroxide ions. In this experiment the kinetics of
the reaction catalyzed by HCl will be studied. HCl
also suppresses the ionization of acetic acid so as
not to change the concentration of hydronium ions
present.
8/4/2019 Expt 6 - Chemical Kinetics
http://slidepdf.com/reader/full/expt-6-chemical-kinetics 2/5
MAPUA INSTITUTE OF TECHNOLOGY
School of Chemical Engineering, Chemistry, Biological Engineering, and Material Science and Engineering
Physical Chemistry Laboratory 2 - 3rd
Quarter SY 2010-2011
Neil Patrick P. Tangara , 3rd
Year B.S. Chemical Engineering
Experiment 6 │ Group 5 │ March 1, 2011 2 of 5
METHODOLOGY
To determine the effect of concentration
and temperature on the reaction mechanism, tworuns of difference concentrations were made at
25oC (assuming room temperature) and one run
was made at 35oC.
The concentration of methyl acetate at a
given time and temperature was determined
through titration of samples with a standard
sodium hydroxide solution since concentration
varies with temperature (25 and 35 oC).
A test tube containing about 12 ml methylacetate was set into a thermostat at 25° C.
Approximately 250 ml of standardized 1 N
hydrochloric acid was placed in a flask clamped in
the thermostat. After thermal equilibrium has been
reached (10 or 15 min should suffice), two or three
5-ml aliquots of the acid were titrated with the
standard sodium hydroxide solution to determine
the exact molarity of the sodium hydroxide in
terms of the standardized hydrochloric acid. Then
50 ml and 100ml of acid was transferred to each of
two 250-ml flasks clamped in the thermostat and 5
min allowed for the reestablishment of thermal
equilibrium. Precisely 5 ml of methyl acetate was
next transferred to one of the flasks with a clean,
dry pipette; the timing watch was started when the
pipette is half emptied. The reaction mixture is
shaken to provide thorough mixing.
A 5-ml aliquot was withdrawn from the
flask as soon as possible and run into 50 ml of
distilled water. This dilution slows down the
reaction considerably, but the solution should be
titrated at once; the error can be further reducedby chilling the water in an ice bath. The time at
which the pipette has been half emptied into the
water in the titration flask is recorded, together
with the titrant volume. Additional samples were
taken at 10-min intervals for an hour; then at 20-
min intervals for the next hour and a half. The
average values were determined by processing
samples for 1 hour and 3 hour intervals.
In similar fashion, another run was madeon a temperature of 35°. Because of the higher
rate of reaction, three samples are first taken at 5-
min intervals, then several at 10-min intervals, and
a few at 20-min intervals. To get the average
values, a 1 hour interval run was made.
RESULTS AND DISCUSSIONS
A. At Room Temperature and Low Concentration
Reaction
Time,
minutes
Volume
NaOH
used, mL
Conc.
Acetic Acid,
M
Conc.
Methyl
Acetate
left, M
0 2.7 0.2847 0.8532
10 2.9 0.3058 0.8321
20 3.0 0.3164 0.8216
30 4.0 0.4218 0.7161
40 4.2 0.4429 0.6950
50 4.3 0.4535 0.6845
60 4.5 0.4745 0.6634
80 4.6 0.4851 0.6529
100 4.9 0.5167 0.6212
120 5.1 0.5378 0.6001
180 5.4 0.5695 0.5685
360 6.2 0.6538 0.4841
Results show that methyl acetate is being
consumed as it is in the reactant side while acetic
acid is being produced as it is in the product side.
More NaOH was used as the reaction further took
place since the concentration of acetic acid
increases with time and thus, requiring more NaOH
to reach its equivalence point during titration.
This part will give us the basis of
comparison later on in the determination of the
8/4/2019 Expt 6 - Chemical Kinetics
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MAPUA INSTITUTE OF TECHNOLOGY
School of Chemical Engineering, Chemistry, Biological Engineering, and Material Science and Engineering
Physical Chemistry Laboratory 2 - 3rd
Quarter SY 2010-2011
Neil Patrick P. Tangara , 3rd
Year B.S. Chemical Engineering
Experiment 6 │ Group 5 │ March 1, 2011 3 of 5
effect of increasing the amount of catalyst (HCl)
present and of increasing the temperature of the
reaction vessel. Two theories (kinetic and collision)
shall be the basis for comparison.
B. At Room Temperature and High Concentration
Reaction
Time,
minutes
Volume
NaOH
used, mL
Conc.
Acetic Acid,
M
Conc.
Methyl
Acetate
left, M
0 2.8 0.4060 0.3763
10 3.1 0.4495 0.3328
20 3.3 0.4785 0.303830 3.5 0.5075 0.2748
40 3.6 0.5220 0.2603
50 3.9 0.5655 0.2168
60 4.2 0.6090 0.1733
80 4.5 0.6525 0.1298
100 4.7 0.6815 0.1008
120 4.8 0.6960 0.0863
180 5.0 0.7250 0.0573
360 5.1 0.7395 0.0428
As compared to part A, part B, having a
higher concentration of catalyst (100ml versus
50ml), have had a faster rate of reaction as evident
on the higher concentration of acetic acid
produced after initiating the reaction at time 0
until time equals 6 hours.
The catalyst works by providing the
optimal conditions for a reaction to occur. The
more catalyst there is, the more contact with the
reactants there is, thus, increasing the rate of
reaction until it reaches its maximum speed.
However, adding too much catalyst on the system
might not help hasten the reaction rate especially
when it already dilutes the system from its optimal
reaction conditions with useless catalyst sites.
This proves the capacity of the catalyst to
initiate and hasten the rate of reaction by
providing the best possible reaction conditions that
require minimal activation energy.
C. At High Temperature and Low Concentration
Reaction
Time,
minutes
Volume
NaOH
used, mL
Conc.
Acetic Acid,
M
Conc.
Methyl
Acetate
left, M
0 2.1 0.4779 0.6600
10 2.5 0.5690 0.5690
20 2.7 0.61445 0.523530 3.1 0.7055 0.4324
40 3.4 0.7738 0.3641
50 3.7 0.8421 0.2959
60 4.0 0.9104 0.2276
80 4.2 0.9559 0.1821
100 4.7 1.0697 0.0683
120 4.8 1.0924 0.0455
180 4.9 1.1152 0.0228
The effect of increasing the temperature
was studied in this part. It was found that it made
the rate of reaction faster as evident on the higher
concentrations of acetic acid produced as
compared to part A (35 versus 25 oC).
Increasing the temperature increases the
kinetic energy of the molecules (kinetic theory).
The more energy there is, the more the molecules
move, thus, increasing the number of collisions
taking place in the reaction vessel. The more
collisions there is, the more the reactants react,
thus, leading to a faster rate of reaction compared
to “non-excited” molecules (collision theory).
CONCLUSION
In summary, the rate of reaction was found
to be dependent on several factors such as the
8/4/2019 Expt 6 - Chemical Kinetics
http://slidepdf.com/reader/full/expt-6-chemical-kinetics 4/5
MAPUA INSTITUTE OF TECHNOLOGY
School of Chemical Engineering, Chemistry, Biological Engineering, and Material Science and Engineering
Physical Chemistry Laboratory 2 - 3rd
Quarter SY 2010-2011
Neil Patrick P. Tangara , 3rd
Year B.S. Chemical Engineering
Experiment 6 │ Group 5 │ March 1, 2011 4 of 5
concentration, catalyst, temperature and other
parameters such as pressure and surface area
which were kept constant throughout the
experiment.
It was found that increasing the amount of
catalyst hastens the rate of reaction by providing
the optimum reaction conditions, that is, by
lowering the activation energy needed for the
reaction to initiate.
It was also found that increasing the
temperature hastens the rate of reaction as well by
providing the molecules more kinetic energy which
leads to more collisions within the system whichinitiates reactions faster as based on kinetic and
collision theories of chemistry.
APPENDICES
Preliminary Data Sheet
*Please refer to the attached document for the
preliminary data sheet.
Kinetics Graphs
*Please refer to the attached document for the
graphs.
Sample Computations
Given: Hydrolysis of Methyl Acetate
Vol. of 1.16 M HCl = 50 ml
Vol. of water = 50 ml
Vol. of MeAc = 10 ml
Required: concentration of HCl in mixture
Solution:
⁄ ()
= 0.527272727 M
Given: Hydrolysis of Methyl Acetate
K1 (low conc.) = 0.0041
K2 (high conc.) = 0.00004
K3 (high temp.) = 0.00003
Required: activation energy
Solution: Arrhenius Equation
[
]
Substituting the values,
[
]
⁄
REFERENCES
Knight, S.B, Crockford, H.B., Fundamentals of
Physical Chemistry 2nd ed., Wiley International,
1964, {Accessed: 02-26-11}
Atkins, Physical Chemistry 5th
edition, chapter 24,
page 841, W.H. Freeman & Company, {Accessed:02-26-11}
Part A: Hydrolysis Rate at Room Temperature and Lower Concentration of HCl
8/4/2019 Expt 6 - Chemical Kinetics
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MAPUA INSTITUTE OF TECHNOLOGY
School of Chemical Engineering, Chemistry, Biological Engineering, and Material Science and Engineering
Physical Chemistry Laboratory 2 - 3rd
Quarter SY 2010-2011
Neil Patrick P. Tangara , 3rd
Year B.S. Chemical Engineering
Experiment 6 │ Group 5 │ March 1, 2011 5 of 5
y = -0.002x + 0.8144R² = 0.8665
0
0.2
0.4
0.6
0.8
1
0 50 100 150
time,min
Zero Order
y = -0.0029x - 0.2019R² = 0.8925
-0.6
-0.5
-0.4
-0.3
-0.2
-0.1
00 50 100 150
l n Y b
time, min
1st Order
y = 0.0041x + 1.218R² = 0.9163
0
0.5
1
1.5
2
0 50 100 1
1 / y b
time,min
2nd order
y = -0.0004x - 2.4539R² = 0.7709
-0.6
-0.5
-0.4
-0.3
-0.2
-0.1
0
0 50 100 150
l n Y b
time, min
1st Order
y = 0.0042x + 1.2056R² = 0.9122
0
0.5
1
1.5
2
0 50 100 1
1 / y b
time,min
2nd order
y = -0.0003x + 2.4643R² = 0.8412
-5
-4
-3
-2
-1
0
0 50 100 150 200
1st order
y = -0.0051x + 11.634R² = 0.7638
0
0.2
0.4
0.6
0.8
1
0 50 100 150 m o l e s a c e t i c a c i d ,
Y b
time,min
Zero Order
Part B: Hydrolysis Rate at Room Temperature and Higher Concentration of HCl
Part C: Hydrolysis of Rate at High Temperature and Lower Concentration of HCl
y = -0.0037x + 11.754R² = 0.8378
-0.2
0
0.2
0.4
0.6
0.8
0 50 100 150 200
zero order
y = 3E-05x + 0.0851
R² = 0.8446
-10
0
10
20
30
40
50
0 50 100 150 2
2nd order