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International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4726
Estimation of Parameters of Kinetic Study and Arrhenius Equation for
the Reaction between Ethyl Acetate with Sodium Hydroxide
Harsh Shah1, Setukumar Vavadiya2, Akshay Dholariya3, Bhaumik Patel4, Kasim Vohra5#
1234 UG Scholars, Chemical Engineering Department, Veerayatan Institute of Engineering, Gujarat, India.
5#Asst. Professor & Guide, Chemical Engineering Department, Veerayatan Institute of Engineering, Gujarat, India.
---------------------------------------------------------------------***---------------------------------------------------------------------
Abstract - Hydrolysis reaction of ethyl acetate and sodium
hydroxide was carried at different temperature and calculate
the conversion of NaOH and also find out the reaction order
and activation energy of particular reaction. The maximum
conversion of NaOH was 96% at 36oC temperature and the
order of reaction for present reaction was best fitted for 2nd
order reaction with respect to sodium hydroxide. The
activation energy of reaction was calculated by Arrhenius
equation, E= 16.20 kcal/mol and frequency factor was ko =
1.85 * 1012. The enthalpy and Gibbs free energy of present
reaction was also calculated bytheoretical methodatdifferent
reaction temperature.
Key Words: Ethyl Acetate, Sodium Hydroxide, Kinetic
Study, Activation Energy, Thermodynamic Analysis.
1. INTRODUCTION
All chemical processes features reactions as the essential
step. Understanding of these reactions plays the vital role in
decision making regarding the choice of reactor, the size of
the reactor, magnitude of operating parameters; etc. An
operational as well as theoretical insight of any reaction
resides in the kinetic study of thoseparticularreactions.This
study yields certain guiding parameters; namely, rate of
reaction, activation energy, rate constant. Theseparameters
allows for the design of scaled up reactor. It also makes it
possible to incorporate some modification within reactor
unit.
This project work aims to carry out the kinetic study of
hydrolysis reaction involving Ester acetate. Reaction is also
known as saponification reaction as it produces sodium salt
after completion.
In this reaction, Alkali breaks the ester bonds to release the
fatty acid. This is one of the most useful reactions in many
chemical industries; pharmaceuticals, food industries, and
others. [1] In this experimental study,ethyl acetateisusedas
the main reactant. In Chemical and food industry it is used
as solvent. [2]
The product Sodium Acetate is alsousedinclearingpurpose.
The special characteristic of sodium Acetate is “Hot ice”.it is
crystalline form of sodium Acetate. In making hot ice we are
using sodium tri sulphite in place of sodium Acetate to
generate Super Saturated salutation. Sodiumacetateused as
salty vinegar test in chips and also as a sealing agent in
concrete. [3]
This work revolves around three key words; reaction,
hydrolysis and kinetic study. The following paragraph
expands on these three terms:
A process in which Raw Material areconvertedinto
the product that Reaction is called Chemical
Reaction. And Study of the parameter such as
reaction-order, reaction constant and the effect of
temperature, concentration, temperature and
agitation on these parameters.
Now second fundamental term is the Difference
between “Hydration Process” And “Hydrolysis
process” .When the process is carriedbyAdditionof
water molecular is called “Hydration Process”while
the compound is broken by water moleculeiscalled
“hydrolysis process”. [4]
Reaction kinetics is the study of rates of chemical
processes. Chemical kinetics involves investigation
of how different experimental condition can
influence the rate and yield information about the
reaction mechanism and transition stage, as well as
the construction of mathematical models.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4727
Chemical reaction takes place when a detectable number of
molecules of one or more species have lost theiridentityand
assumed a new form by a change in the kind or number of
atoms in the compound and by a change in structure or
configuration of these atoms. In this classical approach to
chemical change, it is assumed that the total mass is neither
created nor destroyed when a chemical reaction occurs.
Chemical kinetics is the part of physical chemistry that
studies reaction rates. The reaction rate for a reactant or
product in a particular reaction is intuitively defined as how
fast a reaction takes place. For example, oxidation of iron
under the atmosphere is a slow reaction which can take
years, but the combustion of butane in a fire is a reaction
that takes place in seconds.
2. EXPERIMENTAL SECTION
2.1 Method
First of all weprepare 500 ml of the 0.3 N Ethyl Acetate,0.2N
Sodium hydroxide and 0.2 N Hydrochloric Acid was the first
step of experimental work. Thereafter; 150 ml of 0.3 N Ethyl
Acetate was taken in the reaction beaker and this solution
was heated up to desired temperature(300oCforfirstrun)in
the water bath. Sodium hydroxide, heated up to same
temperature as ethyl acetate, was poured into reaction
beaker containing ethyl acetate. 10 ml ofsolutionwasdrawn
out from the reaction mixture for titration after every two
minutes for the titration--against 0.2 N Hydrochloric Acid.
Similarly, the experiments were carried out to record the
consumption of sodium hydroxide in thishydrolysisreaction
occurring at different temperature; 30, 32, 36 degreeCelsius.
The same procedure was carried out to analyze the effect of
stirring. During that particular run, reaction was allowed to
carry out under stirring effect, imparted by magnetic stirrer.
2.2 Calculations
The consumption of sodium hydroxide was tracked by
mean of volumetric titration. The amount of acid went in to
titration was substituted into the following equation to
determine the amount of sodium hydroxide present at
particular time.
Where, = Normality of NaOH
= Volume of mixture
= normality of HCL
= Volume of HCl used For titration
Then for % conversion of Ethyl Acetate= 1- × 100, [5]
Where, Ca = Concentration of reactant at different reaction
time
Cao = Initial Concentration of reactant
3. RESULTS AND DISCUSSIONS
3.1 Effect of reaction temperature
The reaction was studied at different reaction temperature
and calculate the conversion of NaOH with time. The
maximum conversion was 95% at 14 minutes time.
Conversion of NaOH at differenttemperaturewith respectto
time are showed in figure 1.
0 2 4 6 8 10 12 14 16
65
70
75
80
85
90
95
ConversionofNaOH,XNaOH
(%)
Time (min)
30
o
C
32
o
C
36
o
C
Fig -1: Plot of conversion of NaOH vs time at different
temperatures.
3.2 Kinetic studies
Kinetics of hydrolysisofethyl acetatewithsodiumhydroxide
has been extensively studied. The kinetic profile of given
reaction showed thecontinuousdecreaseinconcentrationof
sodium hydroxide with time as show in figure 2.
The rate of reaction is defined as thechangeinthenumberof
molecules of reacting species per unit volume per unit time.
It is also defined to be proportional to the concentration of
reacting species raised to a certain power called the order of
reaction. It is usually taken as the rate at which the reactant
disappear or the rate at which the product is formed.
The concept of rate of reaction is very important in
evaluating chemical reacting systems. It is the core factor in
the development ofperformancemodelstostimulatereactor
functional parameters.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4728
2 4 6 8 10 12 14
0.01
0.02
0.03
0.04
0.05
0.06
0.07
ConcentrationofNaOH,CNaOH
(mol/lit)
Time (min)
30
o
C
Fig -2: Plot of concentration of NaOH vs time.
Rate constant: Rate constant, K quantifies the speed of a
chemical reaction. ForachemicalreactionwheresubstanceA
and B are reacting to produce C, the reaction rate has the
form
A + B C
R = k [A]m[B]n
Where, k is the rate constant that depends on
temperature. A is the concentration of substance A in moles
per volume of solution assuming the reaction is taking place
throughout the volume of the solution.
Rate constant is the rate of reaction when the
concentration of each reaction istakenasunity.Thatiswhyit
is also known as specific reaction rate. It is a measure of the
rate of reaction, so the greater the value of the rate constant,
the faster the reaction. Each reaction has a definite value of
the rateconstant at a particular temperatureandthevalueof
the rate constant for the same reaction changes with
temperature and the values do not depend upon the
concentration of reaction butdepend upon order of reaction.
The hydrolysis of ethyl acetate illustrates a bimolecular
reaction that gives sodium acetate and ethanol as the product
from which second order rate constant can be calculated:
EA + NaOH SA + Eth
As the reaction proceeds, each hydroxide ion removed in
the formation of ethanol removes one molecule of ethyl
acetate, being the number of moles of either OH- or ethyl
acetate so removed, the concentration of the reactants
decreases. If we start with equal concentrations of the
reactants, the concentration of NaOH can be conveniently
followed atdifferenttimeintervalsbywithdrawinganaliquot
from the reaction mixtureanddeterminingtheNaOHpresent
in it direct or indirect titration with a standard solution of an
acid. The fact that it is a second order reaction can be
established by the consistency of the values of k determined
by substituting the titration resultsat differenttimeintervals
in the second order rate equation.
In order to quantify the reaction order, rate constant and
activation energy, sets of lab-scale experiments were carried
out. In these experiments, two reactants; ethyl acetate and
sodium hydroxide were made to react at different
temperature; 30, 32, 36 degrees Celsius etc. The progress of
reaction was tracked by findingtheconsumptionofreactants
with respect to time by mean of acid-base titration.
The second order rate constant with respect to
consumption of NaOH was also calculated at different
temperatures by plotting 1/CNaOH with time using following
equations, [5] which gives best fit for second order kinetic as
shows in figure 3:
2 4 6 8 10 12 14
0
20
40
60
80
100
1/CNaOH
(lit/mol)
Time (min)
30
o
C, R
2
= 0.90
32
o
C, R
2
= 0.97
36
o
C, R
2
= 0.97
Fig -3: Second order rate constant plot of 1/CNaOH vs
time.
Obtained value of rate constant “k” allows for the
determination of Arrhenius parameters like; activation
energy and frequency factor. Plot of logarithm of k against
the temperature yields the straight line. The slop of the
straight –line equals the factor E/R; while the intercept
represent the frequency factor.
The Arrhenius equation was fitted to therateconstantvalues
at various temperatures. The equation is, [5]
lnk= -
Where, E (kcal/mol) = activation energy, k0 = frequency
factor. The Arrhenius equation was fitted to the rate
constant values at three different temperatures and showed
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4729
good fitness of lnk versus 1/T in figure 4. The activation
energy was found to be E=16.20 kcal/mol with frequency
factor 1.85×1012 for the given reaction.
0.00324 0.00326 0.00328 0.00330
1.3
1.4
1.5
1.6
1.7
1.8
1.9
lnk
1/T (K
-1
)
E = 16.20 kcal/mol, R
2
= 0.99
k0
= 1.85 * 10^12
Fig -4: Arrhenius plot for activation energy.
The final expression for the rate constant can be written as,
3.2 Thermodynamic analysis
Thermodynamic analysis can lead to a better understanding
of the overall performance of any chemical reaction. The
thermodynamic properties of given reaction were also
studied.
Over all reaction is,
EA + NaOH SA + Eth
We calculate the enthalpy of formation of reaction at
standard state. For this we need enthalpy of formation of
substrates and products at T= 298 K.
= -445 kJ mol-1 [6]
= -427 kJ mol-1 [7]
= -709.32 kJ mol-1 [8]
= -235.3 kJ mol-1 [9]
/mol (Reaction is Exothermic)
By using following equation, we calculatetheoreticallyGibbs
free energy for this reaction at standard condition (T=298
K),
= -251.12 kJ mol-1 [10]
= -380.7 kJ mol-1 [7]
= -607.7 kJ mol-1 [8]
= -170.86 kJ mol-1 [11]
-1 (Spontaneous reaction in
forward direction)
Now,
As the reaction approaches equilibrium, becomes less
negative and finally reaches zero. At equilibrium [12]
and Qc = Keq , so we can write
K eq= exp ( )
At 298 K,
Keq = 5.27 * 1025
After that,
ln = -
By using above equation we canabletocalculateequilibrium
constant at different temperature. The graph of Gibbs free
energy and equilibrium constant at different reaction
temperatures are shown in figure 5 & 6. Higher value of
equilibrium constant resulting in higher concentration of
product same thing are experimentally proved by getting
95% conversion of NaOH.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4730
302 303 304 305 306 307 308 309 310
-35.75
-35.70
-35.65
-35.60
-35.55
-35.50
-35.45
-35.40
-35.35
Gibbsfreeenergyofreaction(kcal/mol)
Temp (K)
Fig -5: Plot of Gibbs free energy of reaction vs Temperature.
302 303 304 305 306 307 308 309 310
1.80E+025
2.00E+025
2.20E+025
2.40E+025
2.60E+025
2.80E+025
3.00E+025
3.20E+025
3.40E+025
EquilibriumConstant
Temp (K)
Fig -6: Plot of equilibrium constant vs Temperature.
4. CONCLUSIONS
Findings of the experiments reveal that the hydrolysis
reaction involving sodium hydroxide and ethyl acetate
follows second order kinetics.Thevalueofreactionconstant,
k, increases with temperature up to 36oC. It leads to the
conclusion that the temperature ranging from 30-34 is
critical for efficient conversion. Besides, this study has also
demonstrated the adverse effect of stirring on overall
reaction yield, which means that the reaction rate cannot be
enhanced by stirring; However, lower value of activation
energy for this particular reaction lend itself to the
enhancement by the use of appropriate catalyst. Higher
value of equilibrium constant and lower value of Gibbs free
energy also corroborate the fact to get maximumconversion
of NaOH, 95 % in very less time around 14 minutes at 36oC
for the given reaction.
ACKNOWLEDGEMENT
This work was carried out at Veerayatan Institute of
Engineering, Gujarat, India. The authors are thankful to Mr.
Sagar Jani, HOD of Chemical Engineering Department and
other faculty members Mr. Vijay Patel, Mr. Milind Matang
& Ms. Megha Chhatbar for sharing their pearl of wisdom
during the course of this research work. Authors are also
special thankful to Mr. Milind Matang for helping in editing
the research paper.
ABBREVIATIONS
EA - Ethyl acetate
SA - Sodium acetate
Eth - Ethanol
NOTATIONS
- Enthalpy of formation of ethyl acetate at standard
state
- Enthalpy of formation of sodium hydroxide at
standard state
- Enthalpy of formation of sodium acetate at standard
state
- Enthalpy of formation of ethanol at standard state
- Enthalpy of reaction at 298 K
- Gibbs free energy of ethyl acetate at standard state
- Gibbs free energy of sodium hydroxide at
standard state
- Gibbs free energy of sodium acetateatstandardstate
- Gibbs free energy of ethanol at standard state
- Gibbs free energy of reaction at 298 K
Keq - Equilibrium constant
REFERENCES
1) Ahmad Mukhtar, Umar Shafiq, Ali Feroz Khan, Hafiz
Abdul Qadir and Masooma Qizilbash, Estimation of
Parameters of Arrhenius Equation for Ethyl Acetate
Saponification Reaction, Research Journal of Chemical
Sciences, Vol. 5(11), 46-50, November (2015)
2) Obi Chidi* and Okoye Ifedi Peter, Kinetics and
Mechanism of Ethyl Acetate Production Using Eco-
Benign Solid Catalyst, DOI: 10.4172/2161-
0398.1000219, J Phys Chem Biophys 2016
3) https://www.amazingrust.com/Experiments/how_to/H
ot-Ice.html
4) http://pediaa.com/difference-between-hydrolysis-and-
hydration/
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4731
5) Octave Levenspiel, Chemical Reaction Engineering, 3rd
edition, Willey India Pvt. Ltd, 13, August (1998)
6) https://en.wikipedia.org/wiki/Ethyl_acetate_(data_page
), 19th March, 2019
7) https://en.wikipedia.org/wiki/Sodium_hydroxide,19th
March, 2019
8) https://en.wikipedia.org/wiki/Sodium_acetate, 19th
March, 2019
9) https://en.wikipedia.org/wiki/Ethanol_(data_page),
19th March, 2019
10) https://www.chemeo.com/cid/57-231-
2/Ethyl%20acetate
11) https://www.chemeo.com/cid/35-653-8/Ethanol
12) Smith, J. M., & Van, N. H. C. (1959). Introduction to
chemical engineering thermodynamics. New York:
McGraw-Hill.
BIOGRAPHIES
Mr. Harsh Shah is a 4th year student
of B.E. in chemical engineering
branch at Veerayatan Institute of
Engineering, Gujarat, India
Mr. Setukumar Vavadiya is a 4th
year student of B.E. in chemical
engineering branch at Veerayatan
Institute of Engineering, Gujarat,
India
Mr. Akshay Dholariya is a 4th year
student of B.E. in chemical
engineering branch at Veerayatan
Institute of Engineering, Gujarat,
India
Mr. Bhaumik Patel is a 4th year
student of B.E. in chemical
engineering branch at Veerayatan
Institute of Engineering, Gujarat,
India
Mr. Kasim Vohra is an Assistant
Professor at Chemical Engineering
Department, VeerayatanInstituteof
Engineering. He obtained his M.E.
degree in Chemical Engineering
(2016) from Gujarat Technological
University and Advance post
graduate diploma in Piping Design
(2014) from MIT, Pune, India. In
2013 he completed his graduation
in Chemical Engineering from
Gujarat Technological University,
Gujarat, India. His research interest
includes Kinetic Studies,
Thermodynamic Studies, Synthesis
of Chemicals,andChemical Reaction
Engineering.

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IRJET- Estimation of Parameters of Kinetic Study and Arrhenius Equation for the Reaction between Ethyl Acetate with Sodium Hydroxide

  • 1. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4726 Estimation of Parameters of Kinetic Study and Arrhenius Equation for the Reaction between Ethyl Acetate with Sodium Hydroxide Harsh Shah1, Setukumar Vavadiya2, Akshay Dholariya3, Bhaumik Patel4, Kasim Vohra5# 1234 UG Scholars, Chemical Engineering Department, Veerayatan Institute of Engineering, Gujarat, India. 5#Asst. Professor & Guide, Chemical Engineering Department, Veerayatan Institute of Engineering, Gujarat, India. ---------------------------------------------------------------------***--------------------------------------------------------------------- Abstract - Hydrolysis reaction of ethyl acetate and sodium hydroxide was carried at different temperature and calculate the conversion of NaOH and also find out the reaction order and activation energy of particular reaction. The maximum conversion of NaOH was 96% at 36oC temperature and the order of reaction for present reaction was best fitted for 2nd order reaction with respect to sodium hydroxide. The activation energy of reaction was calculated by Arrhenius equation, E= 16.20 kcal/mol and frequency factor was ko = 1.85 * 1012. The enthalpy and Gibbs free energy of present reaction was also calculated bytheoretical methodatdifferent reaction temperature. Key Words: Ethyl Acetate, Sodium Hydroxide, Kinetic Study, Activation Energy, Thermodynamic Analysis. 1. INTRODUCTION All chemical processes features reactions as the essential step. Understanding of these reactions plays the vital role in decision making regarding the choice of reactor, the size of the reactor, magnitude of operating parameters; etc. An operational as well as theoretical insight of any reaction resides in the kinetic study of thoseparticularreactions.This study yields certain guiding parameters; namely, rate of reaction, activation energy, rate constant. Theseparameters allows for the design of scaled up reactor. It also makes it possible to incorporate some modification within reactor unit. This project work aims to carry out the kinetic study of hydrolysis reaction involving Ester acetate. Reaction is also known as saponification reaction as it produces sodium salt after completion. In this reaction, Alkali breaks the ester bonds to release the fatty acid. This is one of the most useful reactions in many chemical industries; pharmaceuticals, food industries, and others. [1] In this experimental study,ethyl acetateisusedas the main reactant. In Chemical and food industry it is used as solvent. [2] The product Sodium Acetate is alsousedinclearingpurpose. The special characteristic of sodium Acetate is “Hot ice”.it is crystalline form of sodium Acetate. In making hot ice we are using sodium tri sulphite in place of sodium Acetate to generate Super Saturated salutation. Sodiumacetateused as salty vinegar test in chips and also as a sealing agent in concrete. [3] This work revolves around three key words; reaction, hydrolysis and kinetic study. The following paragraph expands on these three terms: A process in which Raw Material areconvertedinto the product that Reaction is called Chemical Reaction. And Study of the parameter such as reaction-order, reaction constant and the effect of temperature, concentration, temperature and agitation on these parameters. Now second fundamental term is the Difference between “Hydration Process” And “Hydrolysis process” .When the process is carriedbyAdditionof water molecular is called “Hydration Process”while the compound is broken by water moleculeiscalled “hydrolysis process”. [4] Reaction kinetics is the study of rates of chemical processes. Chemical kinetics involves investigation of how different experimental condition can influence the rate and yield information about the reaction mechanism and transition stage, as well as the construction of mathematical models.
  • 2. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4727 Chemical reaction takes place when a detectable number of molecules of one or more species have lost theiridentityand assumed a new form by a change in the kind or number of atoms in the compound and by a change in structure or configuration of these atoms. In this classical approach to chemical change, it is assumed that the total mass is neither created nor destroyed when a chemical reaction occurs. Chemical kinetics is the part of physical chemistry that studies reaction rates. The reaction rate for a reactant or product in a particular reaction is intuitively defined as how fast a reaction takes place. For example, oxidation of iron under the atmosphere is a slow reaction which can take years, but the combustion of butane in a fire is a reaction that takes place in seconds. 2. EXPERIMENTAL SECTION 2.1 Method First of all weprepare 500 ml of the 0.3 N Ethyl Acetate,0.2N Sodium hydroxide and 0.2 N Hydrochloric Acid was the first step of experimental work. Thereafter; 150 ml of 0.3 N Ethyl Acetate was taken in the reaction beaker and this solution was heated up to desired temperature(300oCforfirstrun)in the water bath. Sodium hydroxide, heated up to same temperature as ethyl acetate, was poured into reaction beaker containing ethyl acetate. 10 ml ofsolutionwasdrawn out from the reaction mixture for titration after every two minutes for the titration--against 0.2 N Hydrochloric Acid. Similarly, the experiments were carried out to record the consumption of sodium hydroxide in thishydrolysisreaction occurring at different temperature; 30, 32, 36 degreeCelsius. The same procedure was carried out to analyze the effect of stirring. During that particular run, reaction was allowed to carry out under stirring effect, imparted by magnetic stirrer. 2.2 Calculations The consumption of sodium hydroxide was tracked by mean of volumetric titration. The amount of acid went in to titration was substituted into the following equation to determine the amount of sodium hydroxide present at particular time. Where, = Normality of NaOH = Volume of mixture = normality of HCL = Volume of HCl used For titration Then for % conversion of Ethyl Acetate= 1- × 100, [5] Where, Ca = Concentration of reactant at different reaction time Cao = Initial Concentration of reactant 3. RESULTS AND DISCUSSIONS 3.1 Effect of reaction temperature The reaction was studied at different reaction temperature and calculate the conversion of NaOH with time. The maximum conversion was 95% at 14 minutes time. Conversion of NaOH at differenttemperaturewith respectto time are showed in figure 1. 0 2 4 6 8 10 12 14 16 65 70 75 80 85 90 95 ConversionofNaOH,XNaOH (%) Time (min) 30 o C 32 o C 36 o C Fig -1: Plot of conversion of NaOH vs time at different temperatures. 3.2 Kinetic studies Kinetics of hydrolysisofethyl acetatewithsodiumhydroxide has been extensively studied. The kinetic profile of given reaction showed thecontinuousdecreaseinconcentrationof sodium hydroxide with time as show in figure 2. The rate of reaction is defined as thechangeinthenumberof molecules of reacting species per unit volume per unit time. It is also defined to be proportional to the concentration of reacting species raised to a certain power called the order of reaction. It is usually taken as the rate at which the reactant disappear or the rate at which the product is formed. The concept of rate of reaction is very important in evaluating chemical reacting systems. It is the core factor in the development ofperformancemodelstostimulatereactor functional parameters.
  • 3. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4728 2 4 6 8 10 12 14 0.01 0.02 0.03 0.04 0.05 0.06 0.07 ConcentrationofNaOH,CNaOH (mol/lit) Time (min) 30 o C Fig -2: Plot of concentration of NaOH vs time. Rate constant: Rate constant, K quantifies the speed of a chemical reaction. ForachemicalreactionwheresubstanceA and B are reacting to produce C, the reaction rate has the form A + B C R = k [A]m[B]n Where, k is the rate constant that depends on temperature. A is the concentration of substance A in moles per volume of solution assuming the reaction is taking place throughout the volume of the solution. Rate constant is the rate of reaction when the concentration of each reaction istakenasunity.Thatiswhyit is also known as specific reaction rate. It is a measure of the rate of reaction, so the greater the value of the rate constant, the faster the reaction. Each reaction has a definite value of the rateconstant at a particular temperatureandthevalueof the rate constant for the same reaction changes with temperature and the values do not depend upon the concentration of reaction butdepend upon order of reaction. The hydrolysis of ethyl acetate illustrates a bimolecular reaction that gives sodium acetate and ethanol as the product from which second order rate constant can be calculated: EA + NaOH SA + Eth As the reaction proceeds, each hydroxide ion removed in the formation of ethanol removes one molecule of ethyl acetate, being the number of moles of either OH- or ethyl acetate so removed, the concentration of the reactants decreases. If we start with equal concentrations of the reactants, the concentration of NaOH can be conveniently followed atdifferenttimeintervalsbywithdrawinganaliquot from the reaction mixtureanddeterminingtheNaOHpresent in it direct or indirect titration with a standard solution of an acid. The fact that it is a second order reaction can be established by the consistency of the values of k determined by substituting the titration resultsat differenttimeintervals in the second order rate equation. In order to quantify the reaction order, rate constant and activation energy, sets of lab-scale experiments were carried out. In these experiments, two reactants; ethyl acetate and sodium hydroxide were made to react at different temperature; 30, 32, 36 degrees Celsius etc. The progress of reaction was tracked by findingtheconsumptionofreactants with respect to time by mean of acid-base titration. The second order rate constant with respect to consumption of NaOH was also calculated at different temperatures by plotting 1/CNaOH with time using following equations, [5] which gives best fit for second order kinetic as shows in figure 3: 2 4 6 8 10 12 14 0 20 40 60 80 100 1/CNaOH (lit/mol) Time (min) 30 o C, R 2 = 0.90 32 o C, R 2 = 0.97 36 o C, R 2 = 0.97 Fig -3: Second order rate constant plot of 1/CNaOH vs time. Obtained value of rate constant “k” allows for the determination of Arrhenius parameters like; activation energy and frequency factor. Plot of logarithm of k against the temperature yields the straight line. The slop of the straight –line equals the factor E/R; while the intercept represent the frequency factor. The Arrhenius equation was fitted to therateconstantvalues at various temperatures. The equation is, [5] lnk= - Where, E (kcal/mol) = activation energy, k0 = frequency factor. The Arrhenius equation was fitted to the rate constant values at three different temperatures and showed
  • 4. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4729 good fitness of lnk versus 1/T in figure 4. The activation energy was found to be E=16.20 kcal/mol with frequency factor 1.85×1012 for the given reaction. 0.00324 0.00326 0.00328 0.00330 1.3 1.4 1.5 1.6 1.7 1.8 1.9 lnk 1/T (K -1 ) E = 16.20 kcal/mol, R 2 = 0.99 k0 = 1.85 * 10^12 Fig -4: Arrhenius plot for activation energy. The final expression for the rate constant can be written as, 3.2 Thermodynamic analysis Thermodynamic analysis can lead to a better understanding of the overall performance of any chemical reaction. The thermodynamic properties of given reaction were also studied. Over all reaction is, EA + NaOH SA + Eth We calculate the enthalpy of formation of reaction at standard state. For this we need enthalpy of formation of substrates and products at T= 298 K. = -445 kJ mol-1 [6] = -427 kJ mol-1 [7] = -709.32 kJ mol-1 [8] = -235.3 kJ mol-1 [9] /mol (Reaction is Exothermic) By using following equation, we calculatetheoreticallyGibbs free energy for this reaction at standard condition (T=298 K), = -251.12 kJ mol-1 [10] = -380.7 kJ mol-1 [7] = -607.7 kJ mol-1 [8] = -170.86 kJ mol-1 [11] -1 (Spontaneous reaction in forward direction) Now, As the reaction approaches equilibrium, becomes less negative and finally reaches zero. At equilibrium [12] and Qc = Keq , so we can write K eq= exp ( ) At 298 K, Keq = 5.27 * 1025 After that, ln = - By using above equation we canabletocalculateequilibrium constant at different temperature. The graph of Gibbs free energy and equilibrium constant at different reaction temperatures are shown in figure 5 & 6. Higher value of equilibrium constant resulting in higher concentration of product same thing are experimentally proved by getting 95% conversion of NaOH.
  • 5. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4730 302 303 304 305 306 307 308 309 310 -35.75 -35.70 -35.65 -35.60 -35.55 -35.50 -35.45 -35.40 -35.35 Gibbsfreeenergyofreaction(kcal/mol) Temp (K) Fig -5: Plot of Gibbs free energy of reaction vs Temperature. 302 303 304 305 306 307 308 309 310 1.80E+025 2.00E+025 2.20E+025 2.40E+025 2.60E+025 2.80E+025 3.00E+025 3.20E+025 3.40E+025 EquilibriumConstant Temp (K) Fig -6: Plot of equilibrium constant vs Temperature. 4. CONCLUSIONS Findings of the experiments reveal that the hydrolysis reaction involving sodium hydroxide and ethyl acetate follows second order kinetics.Thevalueofreactionconstant, k, increases with temperature up to 36oC. It leads to the conclusion that the temperature ranging from 30-34 is critical for efficient conversion. Besides, this study has also demonstrated the adverse effect of stirring on overall reaction yield, which means that the reaction rate cannot be enhanced by stirring; However, lower value of activation energy for this particular reaction lend itself to the enhancement by the use of appropriate catalyst. Higher value of equilibrium constant and lower value of Gibbs free energy also corroborate the fact to get maximumconversion of NaOH, 95 % in very less time around 14 minutes at 36oC for the given reaction. ACKNOWLEDGEMENT This work was carried out at Veerayatan Institute of Engineering, Gujarat, India. The authors are thankful to Mr. Sagar Jani, HOD of Chemical Engineering Department and other faculty members Mr. Vijay Patel, Mr. Milind Matang & Ms. Megha Chhatbar for sharing their pearl of wisdom during the course of this research work. Authors are also special thankful to Mr. Milind Matang for helping in editing the research paper. ABBREVIATIONS EA - Ethyl acetate SA - Sodium acetate Eth - Ethanol NOTATIONS - Enthalpy of formation of ethyl acetate at standard state - Enthalpy of formation of sodium hydroxide at standard state - Enthalpy of formation of sodium acetate at standard state - Enthalpy of formation of ethanol at standard state - Enthalpy of reaction at 298 K - Gibbs free energy of ethyl acetate at standard state - Gibbs free energy of sodium hydroxide at standard state - Gibbs free energy of sodium acetateatstandardstate - Gibbs free energy of ethanol at standard state - Gibbs free energy of reaction at 298 K Keq - Equilibrium constant REFERENCES 1) Ahmad Mukhtar, Umar Shafiq, Ali Feroz Khan, Hafiz Abdul Qadir and Masooma Qizilbash, Estimation of Parameters of Arrhenius Equation for Ethyl Acetate Saponification Reaction, Research Journal of Chemical Sciences, Vol. 5(11), 46-50, November (2015) 2) Obi Chidi* and Okoye Ifedi Peter, Kinetics and Mechanism of Ethyl Acetate Production Using Eco- Benign Solid Catalyst, DOI: 10.4172/2161- 0398.1000219, J Phys Chem Biophys 2016 3) https://www.amazingrust.com/Experiments/how_to/H ot-Ice.html 4) http://pediaa.com/difference-between-hydrolysis-and- hydration/
  • 6. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 03 | Mar 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 4731 5) Octave Levenspiel, Chemical Reaction Engineering, 3rd edition, Willey India Pvt. Ltd, 13, August (1998) 6) https://en.wikipedia.org/wiki/Ethyl_acetate_(data_page ), 19th March, 2019 7) https://en.wikipedia.org/wiki/Sodium_hydroxide,19th March, 2019 8) https://en.wikipedia.org/wiki/Sodium_acetate, 19th March, 2019 9) https://en.wikipedia.org/wiki/Ethanol_(data_page), 19th March, 2019 10) https://www.chemeo.com/cid/57-231- 2/Ethyl%20acetate 11) https://www.chemeo.com/cid/35-653-8/Ethanol 12) Smith, J. M., & Van, N. H. C. (1959). Introduction to chemical engineering thermodynamics. New York: McGraw-Hill. BIOGRAPHIES Mr. Harsh Shah is a 4th year student of B.E. in chemical engineering branch at Veerayatan Institute of Engineering, Gujarat, India Mr. Setukumar Vavadiya is a 4th year student of B.E. in chemical engineering branch at Veerayatan Institute of Engineering, Gujarat, India Mr. Akshay Dholariya is a 4th year student of B.E. in chemical engineering branch at Veerayatan Institute of Engineering, Gujarat, India Mr. Bhaumik Patel is a 4th year student of B.E. in chemical engineering branch at Veerayatan Institute of Engineering, Gujarat, India Mr. Kasim Vohra is an Assistant Professor at Chemical Engineering Department, VeerayatanInstituteof Engineering. He obtained his M.E. degree in Chemical Engineering (2016) from Gujarat Technological University and Advance post graduate diploma in Piping Design (2014) from MIT, Pune, India. In 2013 he completed his graduation in Chemical Engineering from Gujarat Technological University, Gujarat, India. His research interest includes Kinetic Studies, Thermodynamic Studies, Synthesis of Chemicals,andChemical Reaction Engineering.