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A Research Proposal
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1
A RESEARCH PROPOSAL ON
THE KINETICS OF DEGRADATION OF SODIUM
LAUROYLSARCOSINATE IN THE PRESENCE OF FENTON’S
REAGENT
BY
OLORUNYOMI JOSEPH FUNSO
SUPERVISOR: DR. O. OWOYOMI
SEPTEMBER, 2012
2
TABLE OF CONTENT
CONTENT PAGE
TITLE 1
ABSTRACTS 3
INTRODUCTION AND LITERATURE REVIEW 4
EXPERIMENTAL SECTION AND PROPOSED METHOD OF RESULT ANALYSIS 8
REFERENCES 18
3
ABSTRACTS
This work will be carried out in order to study the kinetics of degradation of sodium
lauroylsarcosinate in the presence of Fenton’s reagent at low pH and a temperature of 250C in
aqueous medium at predetermined times. Studies have revealed that the rate of
biodegradation of surfactants largely depends on whether the condition is aerobic or anaerobic
as some tend to be persistent under anaerobic conditions, also with the possibility of toxic by-
products being involved. However with advanced oxidation processes such Fenton’s reaction,
there is a complete oxidation of the surfactant to stable inorganic compounds. In this study, the
Fenton’s reagents will be used in varying concentrations but which are much higher than the
initial concentrations of the surfactant. To follow-up the rate of degradation, the surfactant’s
concentrations will be determined spectrophotometrically using methylene blue (a cationic
dye). The surfactant-dye interaction would have been previously studied using the methods of
continuous variation and conductometry in the premicellar regions of the surfactant in order to
determine the stoichiometry of the interaction. However, the rate law will be determined from
the degradation studies.
4
INTRODUCTION AND LITERATURE REVIEW
Surfactants have been defined as a diverse group of compounds that are designed to have
cleaning or solubilization properties (Guang-Guo, 2005; Mousavi et. al., 2011). They generally
consist of a polar head group (which may or may not be charged but is well solvated in water),
and a nonpolar hydrocarbon tail (which is not easily dissolved in water). A simple classification
of surfactants is based on the nature of the polar head. The main classes have been identified
as ionic, nonionic, amphoteric and Germini surfactants (Tadros, 2005).
All surfactants exhibit the tendency to self-associate in order to produce an aggregation
polymer called micelle at the surfactant concentration known as Critical Micelle Concentration
(CMC). For this reason, surfactants have been used to perform various functions in some
processes or products, in contrast to other organic chemicals that may be used to produce
another chemical or product (Rosen, 2004). For instance, the catalytic ability of surfactants for
some reactions has been well established (Olanrewaju et. al., 2007; Samiey and Ashoori, 2011),
surfactants are used in dispersing dyes of low solubility in the textile and printing industry
(Sabina and Span, 2000; Petra, 2004; Halide and Kartal, 2007) and the possible use of
surfactants to effect and accelerate the degradation of the toxic pollutant, Polycyclic Aromatic
Hydrocarbon has been reported (Li and Chen, 2009).
BIODEGRADATION OF SURFACTANTS
Since surfactants are used on a large-scale basis from everyday household use to industrial
cleaning and textile manufacturing, there are concerns regarding their effects, particularly their
biodegradability in the environment and their toxicity to marine organisms. The different types
of surfactants that are now in use are of different rate of biodegradation in the environment.
5
Guang-Guo (2006) noticed that while most classes of surfactants readily biodegrade under
aerobic conditions, some are persistent under anaerobic conditions. Tadros (2004) drew
attentions to the factors upon which the rate of biodegradation depends: surfactant
concentration, the pH of the environment, temperature, solubility of the surfactant in water (as
the soluble ones are more readily biodegradable than the less soluble ones which accumulate in
the lipid compartment of the organism) and the degree of branching of the alkyl chain in the
hydrophobic part of the surfactant (since extensive branching tends to reduce the rate of
biodegradation due to steric hindrance, preventing the surfactant molecule from getting close
to the active site of the enzyme).
EFFECTS OF SURFACTANTS AND THEIR BIODEGRADATION PRODUCTS ON LIVING ORGANISMS
It is a known fact that surfactants pose threat to the aquatic environment (Mehrvar and
Venhuis, 2004; Guang-Guo, 2005). Even at low concentrations, they reduce the surface tension
of water, and therefore may increase the adsorption of organic compounds such as pesticides
and phenols on the skin and membranes of aquatic animals and humans (Othman et. al., 2012).
Lee et. al., (2000) opined that in addition to the toxicity and aesthetic problems that they cause;
they also bring about the obstruction of air transportation from air to water.
Surfactants become more dangerous to aquatic lives when they biodegrade to produce harmful
intermediates and by-products. For instance, alkylphenols (nonylphenol and octylphenols)
which are degradation products of alkylphenol polyethoxylates- a class of widely used nonionic
surfactant-have been reported to have estrogenic effects and also possess the ability to
bioaccumulate in aquatic organisms in anaerobic environments(Guang-Guo, 2005). The
6
eventual conversion of a surfactant into stable inorganic compounds will generally involve
several successive transformations which would depend on the conditions of the environment.
ADVANCED OXIDATION PROCESSES
The numerous factors upon which complete biodegradation of surfactants depend have led to
people to use the advanced oxidation processes which convert any organic compound to stable
inorganic compounds. Mehrvar and Venhuis (2004) discussed some advanced oxidation
techniques as follows:
a. Photocatalytic Degradation of Surfactants: This method uses a catalyst that is chemically
and biologically inert, easily recovered and reusable in the presence of ultra-violet
radiation to oxidize organic pollutants, most especially surfactants. A compound that is
normally used for this purpose is titanium (IV) oxide, TiO2. The rate of reaction is found
to be dependent on the adsorption of the surfactant on the surface of the catalyst in
addition to other optimum conditions (pH and temperature). The process has been
found to be successful in mineralization of surfactants except for the fact that takes a
long time (5 hours to degrade 80% of initial linear alkylbenzene sulphonate at
a���� =254nm). A more efficient technique is the use of hydrogen peroxide instead of
titanium (IV) oxide to oxidize surfactant.
b. Wet Air Oxidation of Surfactants: This degradation technique is suitable for the
treatment of organic or inorganic pollutants dissolved in water. It is dependent on high
temperatures and pressures operating in the range of 174–3200C and 2.17–20.7 MPa,
respectively. At high enough temperatures and pressures, the solubility of oxygen
increases and provides the driving force for oxidation. The source of oxygen is either
7
compressed air or pure oxygen. The high pressures are required to keep the water in a
liquid state. Wet Air Oxidation provides the same oxidative ability as flame combustion
but at much lower temperatures.
c. Sonochemical Oxidation of Surfactants: This technique uses high-frequency sound wave
at high temperatures and pressure to cause homolysis of water to produce radicals (H.
and OH.). The attack of the surfactant molecules by the radicals and thermal
decomposition are the main oxidation pathways. The rates of degradation depend on
the surfactant’s initial concentration.
d. Fenton’s Treatment of Surfactant: The Fenton’s system used in treating a wide variety of
organic pollutants consist of Fe2+
combined with hydrogen peroxide H2O2 under acidic
condition. It has been efficiently used as a chemical process for wastewater treatment
(Hassan et. al., 2008).The Fenton’s reagent can generate a huge amount of hydroxyl
radical with powerful oxidizing ability which attacks the organic substrate. It is highly
efficient but this depends mainly on the hydrogen peroxide concentration, Fe2+
/H2O2
ratio, pH and reaction time. When compared with other advanced oxidation methods, it
is better because its raw materials are cheaper, it does not require expensive
instrumentation and it generates a greater amount of oxidants. The widely accepted
mechanism for the reaction is as follows:
�� + � → ��� + �. + ��
�. + �� → �� + ���
�. + ������� → �������� (Hassan et. al., 2008)
8
THE SCOPE OF THIS WORK
The surfactant that will be used in this study is Sodium lauroylsarcosinate (which would
thereafter be referred to as SNa)
Na+N
O
O-
O
N-lauroylsarcosine, Sodium salt
Sodium lauroylsarcosinate is a surfactant used in a wide range of personal care products such
as in the making of toothpaste and in the cosmetic industry. However, like other surfactants, it
has some environmental effects. Anwal et. al. (1983) reported its disruptive effect on the outer
membrane of Pseudomonas cepacia by altering the fluidity of the outer membrane of the
organism. The degradation of the surfactant will be carried out in the presence of Fenton’s
reagents (Fe (II)/H2O2 system) under specific conditions of pH, temperature and at
predetermined times. To monitor the rate of degradation, the surfactant concentration will be
determined spectrophometrically as earlier described by Smith (1963) and then later by Koga
et.al. (1995) and Kotchi et.al. (2010).
AIM OF THE STUDY
This work will be aimed at studying the kinetics of degradation of sodium lauroylsarcosinate in
the presence of Fenton’s reagent.
9
OBJECTIVES
1. The method of continuous variation will be used to study the interaction between
methylene blue, a cationic dye with the surfactant.
2. Conductometric technique will also be used to study the surfactant-dye interaction and
this technique will be compared with the first one in order to assess the interaction.
3. Fenton’s oxidation of the surfactant will be studied and the rate law for the process will
be derived.
10
EXPERIMENTAL SECTION AND PROPOSED METHOD OF RESULT ANALYSIS
In wastewater analysis and anionic surfactant degradation studies, several techniques such as
microbial sensor, amperometric biosensor, ion-pair formation with insitu flow injection analysis
using dynamic surface tension detection and chromatography have been used to determine the
surfactant content of a given reaction mixture (Pal et. al, 2005; Hassan et. al, 2008), but these
require expensive instrumentation. A simplified spectrophotometric method using
methylthioninium chloride also known as methylene blue (MBCl), a cationic dye, will be used in
the extraction and determination of residual surfactant content in the reaction mixture. This
method relies on the understanding that any surfactant molecule present forms an ion-pair
with the cationic dye and this can be extracted in a suitable organic solvent (Koga et. al., 1995;
Kotchi et. al., 2010).
NS+
N
N
Cl-
Methylthioninium chloride
Reagents: FeSO4.7H2O, H2O2 ,Methylene Blue, Sodium N-Lauroylsarcosine, Chloroform, H2SO4
and NaOH (to control the pH of the Fentons reaction)
11
The Interaction between Methylene Blue (MBCl) and Sodium lauroylsarcosinate (SNa)
Two methods will be employed in studying the interaction between MBCl and SNa in order to
determine their stoichiometric composition in the ion-pair and ion-pair formation constant (Kf).
These are Job’s method of continuous variation and Conductometric technique.
Job’s Method of Continuous variation: This method was initially used to study and determine
the formula and the formation constants of transition metal complexes in solution. It was
originally described by Ostromisslenski in 1911; the principles were outlined by Denison in
1912, but the method was named after Paul Job who in 1928 published a detailed application
of the technique to study a wide range of coordination compounds. This method has been used
by researchers to study the dye-surfactant interaction in recent time (Petra and Span, 1999;
Sinem and Melda, 2003; Petra, 2004). Where only one complex is important and the measured
experimental property depends linearly on concentration, the method is capable of yielding
both the stoichiometric composition and the association constant of the complex. (Petra and
Span, 1999)
Preparation of Solutions for the Determination of Stoichiometry of the Ion-Pair: Equimolar
stock solutions of MBCl and SNa of concentrations �� and �! respectively would be prepared
in the premicellar regions of SNa such that �� = �! = 1.0 × 10�%&�'�&��,3.0 ×
10�%&�'�&��,5.0 × 10�%&�'�&��, 7.0 × 10�%&�'�&��,and 9.0 × 10�%&�'�&��.
The Critical Micelle Concentration (CMC) of SNa is 1.457 × 10�&�'�&�� (Venkataraman
and Subrahmanyam, 1985). The temperature of 250C would be maintained throughout this
study. The absorbance of the solutions of the dye would be taken in order to determine its
12
molar extinction coefficient(Ɛ�). Both solutions of MBCl and SNa would be mixed in a 10 ml
flask in varying volume ratios such that 0 unit volume of SNa is added to(1 − 0) unit volume of
MBCl solution. A series of ten mixed solutions are prepared from each pair of MBCl and SNa
stock solutions. The absorbance A of the mixtures would be taken and recorded.
Determination of Stoichiometric ratio of MBCl and SNa in the Ion-Pair Formed: The
stoichiometry is determined by plotting the corrected absorbance ΔA of particular mixtures
against the volume ratio0 of the surfactant. ΔA represents the difference between the
measured absorbance Aexp and the theoretical absorbance Athe:
34 = 45�6 − 4785 (1)
The theoretical absorbance is the absorbance of the mixture if no reaction has occurred in the
solution, so that:
4785 = Ɛ9:9;(1 − <) + Ɛ=:=;< (2)
Where Ɛd and Ɛs are the molar extinction coefficients of the dye and surfactant respectively, ��
and �! are the stock concentration of the dye and surfactant respectively and 0 is the volume
ratio of the surfactant in the mixture. >?0@ represents the sum of absorbances of all species
existing in the solution.
45�6 = Ɛ9:9 + Ɛ=:= + Ɛ9=:9= (3)
Where Ɛds is the molar extinction coefficient of the dye-surfactant complex (the ion-pair) and
Cds is the concentration of the ion-pair; �! and �� are the concentrations of the free surfactant
and dye molecules respectively.
13
If the absorbances are measured in the visible region of the electromagnetic spectrum where
the surfactant would show no absorption, then we could calculate the corrected absorbance as:
34 = 45�6 − Ɛ9:9;(1 − <) (4)
Studies have revealed that the plot of corrected absorbance, A> against the volume fraction of
the surfactant 0 is a curve with a maximum or minimum at 0 = 0B corresponding to the
combining ratio of the dye and surfactant in the complex (Petra and Span, 1999; Sinem and
Melda, 2003; Petra, 2004).
Determination of Equilibrium Constant of the Ion-Pair: Schaeppi-Treadwell’s Method
Schaeppi-Treadwell’s Method is a derivative of Job’s method of continuous various which will
be used in determining the ion-pair formation constant. It is a suitable method when only one
stable complex is formed; however the method depends on the stoichiometric composition of
the complex (Petra, 2004). Supposing there is a 1:1 formation of ion-pair between the cationic
dye and the anionic surfactant; then the equilibrium constant is:
CD + E� CD − E (5)
The Kf can be obtained from the plot of corrected absorbance, A> against the volume fraction
of the surfactant 0. The measured A> at 0 = 0B is compared to theoretical A>0 which is
derived by extrapolation of the linear parts of the curve to their intersection. The ratio of A> to
A>0 represents the degree of association, (1-β).
FG
FGH= (1 − I) (6)
Kf
14
Where β is the degree of unassociated ions; since the dye and the surfactant are of equal
concentration, then �� = �! =� , then the equilibrium constant expression can now be written
as:
KL =[NO�P]
[NOR][PS]=
(T�U)
(VWXH)UW
=(T�U)
XHUW (7)
T
:; is the concentration of the dye and surfactant in a 1:1 ratio.
Conductometric Approach to Studying Dye-Surfactant Interaction: In order to study the ion-
pair formation between MBCl and SNa, the conductivity measurement would be done at the
premicellar concentrations of the surfactant and at low concentration of the dye. The specific
conductivities of the surfactant and the dye in the absence of the surfactant would be taken for
about thirty different concentrations. The specific conductivity of the dye-surfactant system as
a function of the surfactant concentration would be taken. To obtain the dye-surfactant system,
a solution of the dye would be used to prepare the concentrated stock solution of the
surfactant. All measurement would be taken at 250C.
Determination of Equilibrium Constant: If we assume a 1:1 ion-pair formation, then the
equilibrium reaction would be:
CD + E� CD − E (8)
In order to determine concentration of free and bound surfactant and dye ions as well as the
value of the equilibrium constant, the measured conductivity which is the sum of the
contribution of all free ions in the solution cannot be solely depended upon. A theoretical
K
15
model which describes the condition within the solution must be applied. This model has been
previously used by Bracko and Span (2001), Halide and Kartal (2005), Sibel and Duman (2006)
and more recently Nora (2012) to study various surfactant-dye interaction conductometrically.
The model assumes that the cationic dye MB+ and the anionic surfactant S
- form a non-
conducting ion-pair in the solution.
Based on Kohlrausch’s law, we know that:
ɅNOXZ; = �NOR
; + �XZS; (9a)
and ɅP[�; = �PS
; + �[�R;
(9b)
Where ɅNOXZ; and ɅP[�
; are the equivalence conductances of the dye and surfactant
respectively at infinite dilution; �NOR; , �PS
; , �[�R;
and �XZS; are the equivalent ionic conductances
at infinite dilution. Ʌ values can be determined experimentally from the specific conductivities
of the surfactant and the dye by converting them to equivalent conductance using:
Ʌ =T;S\]
X (10)
Where C is the molar concentration; the values of Ʌ; can be determined by plotting Ʌ
against√:. The intercept of the plot on the Ʌ-axis is the Ʌ;. Using the values of �[�R;
and �XZS;
from the literature, one can write:
�NOR; +�PS
; = ɅNOXZ; + ɅP[�
; − (�[�R; + �XZS
; ) (11)
Then the equilibrium constant can be expressed as:
16
K =[NO�P]
[NOR]`[PS]` (12)
Where[CD − E], [CD]Land [E�]L are the concentrations of ion-pair, free dye and surfactant
ions respectively.
The concentrations of the free ions cannot be easily determined and so, they are expressed in
terms of [CD]7 and[E�]7, the total dye and surfactant concentrations respectively, so that
[E�]7 = [E�]L + [CD − E] and (13a)
[CD]7 = [CD]L +[CD − E] (13b)
The observed specific conductivity abc= can be expressed as sum of specific conductivity of
surfactant a= and the specific conductivity of the dye a9 if there were no surfactant-dye
interaction.
abc= = a= +a9 (14)
This means that before the ion-pair formation, the surfactant-dye interaction is negligible, and
then;
10��abc= = �PS[E�]7 + �[�R[d�]7 + �NOR[CD
]7 + �XZS[:'�]7 (15)
But with the formation of ion-pair, a decrease in the concentration of free ions occur and so
equation (14) can be written in terms of the concentration of the conducting species, free ions.
10��abc= = �PS[E�]L + �[�R[d�]7 + �NOR[CD
]L + �XZS[:'�]7 (16)
17
Since the ion-pair is a non-conducting specie, then equations (13a) and (13b) can be rearranged
to give the concentration of the free ions in terms of the total concentration of the dye and the
ion-pair.
[E�]L = [E�]7 − [CD − E] and (17a)
[CD]L = [CD]7 −[CD − E] (17b)
Equations (17a) and (17b) can be inserted into equation (16) in order to obtain:
10��abc= = �PS([E�]7 − [CD − E]) + �[�R[d�
]7 + �NOR([CD]7 −[CD − E]) + �XZS[:'
�]7
(18)
Subtracting equation (18) from (15) cancels out the total concentration terms and yields the
‘specific conductivity’ of the ion pair:
10��3a = [CD − E](�NOR + �PS) (19)
So that 3a is the difference between the theoretical and measured specific conductivities at a
givien surfactant concentration. Kohlrausch’s law for infinite dilute solution of an electrolyte
can be applied to equation (19) to obtain:
10��3a ≈ [CD − E](�NOR; +�PS
; ) = [CD − E]Ʌ;NO�P (20)
Where Ʌ;NO�P is the equivalent conductance of the ion-pair at infinite dilution, Ʌ;NO�P value
would be determined experimentally by measuring the specific conductivities of the dye and
surfactants.
18
The equilibrium constant can be calculated by inserting equations (17a) and (17b) into equation
(12):
K =[NO�P]
([PS]f�[NO�P])([NOR]f�[NO�P]) (21)
The Gibbs free energy for the ion-pair formation at 250C can be calculated as:
∆h; = −ij'�K (22)
THE FENTON’S REACTION
The degradation studies of Sodium lauroylsarcosinate will be done at relatively lower
concentration of the surfactant than the oxidant concentrations in order to be able to monitor
the reaction rate. The initial concentrations will be at proportions [H2O2]0=100[SNa]0=2[Fe2+
]0 at
a constant temperature of 250C and a pH of 3.
Procedure: An acidified water (pH=3) is used to prepare the surfactant at very low
concentration (below its CMC) and the Iron (II) tetraoxosulphate (VI) salt. Hydrogen peroxide is
freshly prepared in an amber bottle before the start of any experiment. The reaction takes
place in 500 ml vessels that are opaque to light. A calculated volume of Fe2+
solution prepared
is added to the solution of the surfactant and the mixture is then agitated with the aid of
magnetic stirrer. 25 ml of this mixture is taken before the H2O2 is added. This corresponds to
the concentration of the surfactant at time t=0. A known volume of H2O2 is then added to the
remainder. To monitor the reaction progress, 25 ml of the sample after the H2O2 has been
added is taken at various times (t= 1, 5, 15, 30, 45, 60, 90, 120 minutes). The H2O2 is only added
at the beginning of the reaction. Each sample is neutralized by a known amount of sodium
19
hydroxide to stop the reaction at the predetermined time. All samples are brought back to the
working temperature for analysis. The reaction can be repeated at varying concentrations of
the H2O2 and Fe2+
but at constant [SNa]0 in order study the effect of varying Fenton's reagent
concentration on the oxidation of the surfactant.
Analysis of the Samples: Alkaline solutions of chloroform and methylene blue would be added
to each sample. The biphasic solution formed is then shaken thoroughly to ensure the
distribution of the components throughout the organic and aqueous phases. The dye molecules
should form ion-pairs with the residual surfactant molecules in the solution. It has been shown
in an equilibrium studies of anionic surfactants (AS) with methylene blue, and their associated
ion-pair AS-MB in water and chloroform phases, that both AS and MBCl molecules alone are
never transferred to the chloroform phase but are rather associated forming an ion-pair AS-MB
(Koga et. al., 1999). On this basis, the absorbance of the solution (in the chloroform phase) is
then measured at a ����.
Determination of Surfactant concentration in the Samples: The absorbance of the chloroform
phase is related to the surfactant concentration. This relationship can be determined by
drawing a calibration profile. To obtain this, different standard solutions of surfactants are
prepared and each is added to a chloroform- MBCl system. The mixture is agitated; the ion-pair
extracted into the organic phase and the absorbance measurement is made. A plot of
absorbance against the varying concentration of the surfactant gives the relationship between
the measured absorbance and the concentration of the surfactant.
20
Determination of Rate Law: the data obtained would be used to determine the rate law of the
reaction.
21
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