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International Research Journal       ISSN-0975-3486       VOL. I * ISSUE—3&4          RNI : RAJBIL/2009/30097

                                       Research Paper—Science
                          MODELING OF ELECTROCHEMICALLY
                             SYNTHESIZED THIN FILMS OF
                           CONDUCTING POLYMER FOR THE
                             IMMOBILIZATION OF ENZYME
 Dec.-09—Jan.-2010
                                     *Dr. P. A. Savale **Dr. K. G. Chaudhari

       *Department of Physics, Arts and Science College, Bhalod.
     **Department of Chemistry, Arts and Science College, Bhalod.
ABSTRACT
   The model is simplified representation of the real world. The simple model for conducting polymer
   based biosensor system is presented in the present research work. Now days, electrically conducting
   polymers have received great attention as a class of advanced material due to their remarkable
   attributes and new application area in various fields of life. In this work, efforts have been made on
   the description of mathematical modeling of steady-state analysis of mediated amperometric system.
Keywords: Mathematical modeling, conducting polymer, flux
Introduction
     Computer stimulation is ‘experiment’ using reaction takes place, problems in differential calculus
computer to realize meaningful result. It is less costly, will often be encountered. The purpose of the solution
less time consuming and much safer than actual of these differential equation systems will be to provide
physical experiment. Simulation is done in two steps. a description of the behavior of the system in a more
The first step is to build reliable model. Then simulation manageable. Frequently algebraic form, predictive
is performed as the second step with              carefully studies and experimental data analysis can be readily
chosen input and parameter. When the input and performed. Theoretical analysis will involve the
parameter is not appropriate, model and simulation will relatively straightforward process of linking together
give misleading and erroneous result. Simulation helps the different components of the system rather than
in selecting suitable input set and design parameter starting completely afresh [2].
[1]. The advantage of using electrochemically                   Enzymes are biological catalysts and in the
deposited polymers is their ease of preparation and presence of these enzymes biological reaction gets
the uniformity of the prepared films.                       accelerated. These are the specialized group of proteins
     Provision of a formal theoretical description relies having specific three dimensional active structure and
upon the available mathematical tools. Since, in active sites. An enzyme remains active at optimum
considering biosensors, a chemical change will condition of temperature, pH, substrate concentration,
generally be involved. This will most commonly be and enzyme concentration, inhibitors etc. These are
based upon differential calculus, the mathematics of various parameters, which are used to measure the
change. Further, with parameters changing both with rate of enzyme reaction, which involves substrate,
time and with distance from the surface at which the which get converted into product with the help of

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International Research Journal       ISSN-0975-3486         VOL. I * ISSUE—3 &4          RNI : RAJBIL/2009/30097
enzyme. Therefore, the rate of reaction can be measured      can be used for the immobilization of enzyme on an
or determined by either measuring the rate at which          inert electrode. The simplification of this system allows
substrate is consumed or at the rate at which the            us to set all fluxes as equal. This flux must also equate
product is formed [3].                                       with the current for generation of the oxidized mediator
     The specific recognition characteristics of enzyme      at the electrode. By varying substrate concentration
antibodies and general receptor systems are employed         (S∞), we have observed the changes in the observed
to perform a variety of functions within the organisms       flux (1/jobs). The characteristics of the observed flux
from which they are isolated, catalysis, defence,            and the interference effects on its performance have
communication and control being the primary ones.            been predicted.
This specific recognition is based upon chemical             Model Building
binding of the one component to its complementary                  Researchers and engineers are usually develops
partner, this being the target analyte and the biological    physical models called ‘Scale model’. An amperometric
component of the biosensor respectively. This                enzyme substrate electrode with a PO2 basic sensor
chemical binding can be very strong indeed and the           [7], modeling and simulation of a diffusion limited
binding process is frequently very rapid. Whatever           glucose biosensor [8], a coupled two-compartment
the normal function of a biological component within         model for immobilized enzyme electrodes,
an organism, the basic principle behind its capacity         electrochemical immobilization of enzymes [9], for
for specific recognition will be the same and, for our       instance is build to study the measuring range,
current purpose, we need concern ourselves only with         sensitivity and response time of the sensor. Likewise,
the fundamentals of the binding process as it relates        amperometric enzyme electrodes [10], electrochemical
to biosensors [4].                                           immobilization of enzyme electrodes [11] is built by
     Immobilized enzymes are used in many                    researchers and engineers. While these are useful, they
applications both in synthetic and in analytical             are, in most cases, static models. We are often interested
chemistry [5]. Since, the works of Clark and Lyons,          in the dynamic performance of system, before building
hundreds of paper have been published regarding the          the actual prototype. The physical models are difficult
design of practical amperometric enzyme electrodes           to build and can be expensive.
for the analysis of clinically important metabolites and           Most of the models can be structured as three-
industrial monitoring. Among these reports, two kinds        part system. Some input (substrate) is provided,
of problems are always the main subject. One is the          process (enzyme kinetics and chemical reaction) is done
immobilization of enzyme. Different immobilization           and we get some small output (small signal current).
methods and materials have been developed including          Consider the case of the mediated amperometric device.
adsorption, cross-linking, self assembly methods and         This is an example of considerable interest in biosensor
conducting or non-conducting polymers as well as             research. In this type of model, input may be substrate
different types of gels. The aim of all these efforts was    (glucose) and mediator is oxygen. The process starts
to obtain an easy handling method with cheap and             by defining the various elementary steps involved and
stable material, which can retain high biological activity   their rates. The system consists of an electrode, which
of the enzyme. However, a good biosensor depends             monitor and provides the measurement signal. The
not only on a good immobilization method but also on         electrolyte layer, which contains the mediator and the
a sensitive tranducer. This is the other focus in the        enzyme, an outer membrane which serves to control
development of amperometric enzyme electrode [6].            diffusional mass transport to the electrolyte layer as
     In the present research work, efforts have been         well as to physically constrain the electrolyte close to
made on the description of mathematical modeling of          the sensing electrode.
steady-state analysis of mediated amperometric                     The steady state analysis of the mediated
system. This model is presented for electrochemically-       amperometric system illustrating the various transport
polymerized thin films of conducting polymers which          and kinetic processes is shown in Fig.1. Here, the

128
International Research Journal         ISSN-0975-3486        VOL. I * ISSUE—3&4           RNI : RAJBIL/2009/30097
substrate (S) and oxidized form of the enzyme (EO)            Mathematical Structure
reacts with each other and we get enzyme substrate                   Models are built with inter-related set of equations.
complex (EOS). The next step is that this complex (EOS)       These equations may be algebric or differential
gives the product (P) and reduced form of the enzyme          equations and with logical statements for constraints
(ER). By allowing a particular rate of O2, we get, oxidized   and bounds. Consider the case of steady-state analysis
form of enzyme (EO) and reduced form of mediator (MR)         of mediated amperometric system. It is a probabilistic
and at the end at the electrode, reduced form of the          model. By straightforward algebric manipulation, an
mediator gets converted into oxidized form by releasing       expression describing the output signal in terms of the
2e- (electrons). This gives the current at the electrode.     various kinetic parameters characterizing the system
All these reactions have particular rate. These rate          can be derived and the substrate concentration, which
constants are known as enzyme kinetics rate                   it is the purpose of the device to measure. The reaction
constants. They are governed by Michaelis-Menten              sequence upon which the system is based can be
constant (KM).                                                written as follows.




     Figure 1 Steady-state analysis of mediated                    The relation 1 and 2 represents the oxidation of
amperometric system.                                          substrate to product, according to Michaels-Menten
     To begin with models, they are built with a few          kinetics by the oxidized (EO) enzyme to give the reduced
algebraic equations and a few variables. They may             form of the enzyme (ER). The relation 3 represents the
provide a general description of the system. The              reoxidation of the reduced enzyme by oxidized mediator
mathematical model for conducting polymer based               (MO), giving rise to the reduced mediator (MR). The
amperometric sensor can built on the basis of material        relation 4 represents the reoxidation of the mediator at
used for the electrode, enzyme used, method of                an electrode which gives rise to the current upon which
immobilization used, conducting polymer used, size of         the measurement is based. Rates of formation and
the sensor which material it sense and what are its area      disappearance of EoS-complex can be written as,
of applications. More complex models would include
the more than one enzyme immobilized, rate of electron
transfer, rates of various enzyme kinetic reactions and
environmental conditions etc. One of the major                     Where, Vf is the rate of formation and Vd is the
decisions of a model builder is, then, to choose the          rate of disappearance of the bimolecular EoS-complex.
variables to be included in the model and to exclude          The steady state assumptions
“more complex” or less important variables. A model                Consider homogeneous solution enzyme kinetics.
can grow with addition of variables based on                  A steady state is established in which the rates of
interactions with the users.                                  different steps occurring in the electrolyte layer are

çÚUâ¿ü °ÙæçÜçââ °‡ÇU §ßñËØé°àæÙ                                                                                     129
International Research Journal        ISSN-0975-3486         VOL. I * ISSUE—3 &4          RNI : RAJBIL/2009/30097
balanced with one another and with the mass transport         different dependence upon the three concentration
of reactant and product to and from it. The assumption        variables at our control, that of the substrate, enzyme
requires that the sensing reaction cause negligible           and mediator (O2). To test the model experimentally,
change in the bulk solution concentrations of reactant        we keep two of these concentrations (enzyme and
and product. The approximation is valid, provided             mediator) constant change the third and investigate
that the electrolyte layer sufficiently thin so that          the effects on the observed flux. Then, by taking
diffusion times across it are short and that the diffusion    double reciprocal plots and measuring slopes and
rates are relatively rapid as compared with the enzyme        intercepts from them, we can predict results of
reaction rates. We assume that there is an excess of          simulation about the characteristic rate for each step.
mediator and that the electrode generates M0 from MR          When the conducting polymer film is sufficiently thin
sufficiently rapidly that the concentration of M0 is          and there is no concentration polarization of either
effectively that of the total mediator [M]. This              enzyme (S) or oxygen (O2) within the film, then in steady
condition can be arranged in practice by ensuring that        state we can write,
the reoxidation occurs rapidly at the electrode, the
electrolyte layer is thin so that the diffusional mass
transport of mediator across it to the electrode is also
rapid and the mediator concentration is sufficiently in
excess of the enzyme concentration.
     Estimation of flux of the substrate
     Using steady sate assumptions, a rate equation
for the intermediate can be written as,
     d[EoS] /dt = k1[E][S] – k-1[EoS] – k2[EoS] = 0     [5]
     As the total concentration of enzyme [ET], at all
times will be the sum of concentrations in free and
complexed forms [E] + [EoS]. Now, putting [E] = [ET]-
[EoS] in the above equation we get,
     d [EoS]/dt = k1[ET][S]– ( k1[S]+k–1+k2) [EoS] = 0
                                                                   This equation represents the contribution to the
[6]
                                                              rate control by the reaction of reduced enzyme with
                                                              the mediator to generate the oxidized enzyme. Equating
                                                              equations 10 and 11 and solve them, we get,




    Putting this into the rate expression for                        At low substrate concentration, when the term (k
decomposition of the complex to form the product              KA a¥ KM) in the denominator is dominant, js µ S¥. As
gives the rate (v) of product formation,                      the concentration of substrate is increased, either the
    v = k2[EoS]                                               term (KA a¥ KS s¥) or the term (kcat KS S¥) becomes
    v = k2 [ET] [S]/ KM + [S]                                 dominant and js becomes independent of the substrate
                                                              concentration. This can occurs for two reasons. When
                                                              the term (k KA a¥ KS s¥) is dominant, then js is limited by
                                                              the saturated enzyme kinetics for the consumption of
                                                              substrate. When the term (kcat KS S¥) is dominant, then
     In the above expression each term shows a                js is limited by the rate of reoxidation of the enzyme by

130
International Research Journal         ISSN-0975-3486        VOL. I * ISSUE—3&4            RNI : RAJBIL/2009/30097
reaction with the mediator, under these circumstances         the film, it is possible to estimate the kinetics of the
js is depends on a¥.                                          reactions of the immobilized enzyme. This is an
Mathematical Model                                            operational characteristic of value in a biosensor. By
      The flux of the substrate js reacting within the film   varying the enzyme concentration [ET], membrane
is not necessarily the same as the flux of reduced            thickness and k D , one may investigate the
mediator detected at the electrode jobs. This happens         contributions of the rates of the two different steps to
due to some of the mediator will be lost to the bulk          the overall rate. In equation 16, each term shows a
solution. The precise amount will depend on the               different dependence upon the three concentration
efficiency of mass transport of hydrogen peroxide             variables at our control that of the substrate, enzyme
(H2O2) away from the electrode. When this is very             and mediator.
efficient, then the concentration of hydrogen peroxide        Conclusion
(H2O2) held at zero. At the outside of the film, jobs = (js        We have described the mathematical model of the
/ 2). It is assumed that, the experiment is carried out at    steady state mechanism of amperometric system of
the rotating disk electrode; the mass transport of            electrochemically synthesized thin films of conducting
hydrogen peroxide (H2O2) away from the electrode can          polymer on which enzyme was assumed to be
be controlled. We can show that,                              immobilized. The flux from which the measured signal
       jobs = (js / á)                              [13]      obtained is directly proportional to substrate
                                                              concentration. This is an operational characteristic of
                                                              value in an enzyme electrode. One may use
                                                              mathematical model for the development of conducting
                                                              polymer based mediated amperometric system.

                                                              R E F E R E N C E
    Note that, 1 < á < 2, as expected. By combining
                                                                    1)“Computer based modeling and simulation 1. Modeling
equations 12 and 14, we obtain the expression for the         deterministic systems”, N.K. Srinivasan, Resonance, Journal
observed current.                                             of Science education, Volume 6. Number3, March-2001, 46-
    i = nFA js                                                54. 2) “Theoretical methods for analyzing biosensor
    Again, jobs = js á, we get,                               performance”, Mark. J. Eddowes 3) “Elements of
                                                              biochemistry”, H.S. Srivastava. 4) “The organic chemistry of
                                                              enzymes”, Richard B. Silverman, Academic press. 5)
                                                              “Electrochemical immobilization of enzymes Part 1. Theory”
                                                              P.N. Bartlett and R. G. Whitaker. J. Electronal Chem., 224,
                                                              (1987), 27-35. 6) “Self-gelatinizable copolymer immobilized
                                                              glucose biosensor based on Russian Blue modified Graphite
                                                              electrode”, Qing Deng, Bin Li and Shaojun Dong. The Analyst,
                                                              1998, 123, 1995-1999, 1995. 7) “Mathematical simulation
                                                              of an amperometric enzyme substrate electrode with a PO2
                                                              basic sensor. Part 1. Mathematical model and simulation of the
                                                              PO2 basic sensor”, K. Lemke, Medical and Biological engineering
                                                              and computing, Sept. 1988, 523-532. 8) “Modelling and
                                                              Simulation of a diffusion limited glucose biosensor”,
                                                              A.Cambioaso, L. Delfino at el. Sensors and Actuators, B33
                                                              (1996) 203- 207. 9) “Electrochemical Immobilization of
                                                              enzymes.3: Immobilization of GOD in Thin films of
                                                              Electrochemically Polymerized Phenols”, P.N. Bartlett, Peter
                                                              Tebbutt and Claire H. Tyrrell, Anal. Chem., 64, (1992), 138-
     Now, by measuring the current for the enzyme             142. 10) “Amperometric enzyme electrodes: Theory and
coated electrode as a function of the concentrations          Experiments.The use of electrochemical methods in the study
                                                              of modified electrodes”, P. N. Bartlett.
of substrate, mediator and of the enzyme loading in
çÚUâ¿ü °ÙæçÜçââ °‡ÇU §ßñËØé°àæÙ                                                                                        131

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RESEARCH ANALYSIS AND EVALUATION

  • 1. International Research Journal ISSN-0975-3486 VOL. I * ISSUE—3&4 RNI : RAJBIL/2009/30097 Research Paper—Science MODELING OF ELECTROCHEMICALLY SYNTHESIZED THIN FILMS OF CONDUCTING POLYMER FOR THE IMMOBILIZATION OF ENZYME Dec.-09—Jan.-2010 *Dr. P. A. Savale **Dr. K. G. Chaudhari *Department of Physics, Arts and Science College, Bhalod. **Department of Chemistry, Arts and Science College, Bhalod. ABSTRACT The model is simplified representation of the real world. The simple model for conducting polymer based biosensor system is presented in the present research work. Now days, electrically conducting polymers have received great attention as a class of advanced material due to their remarkable attributes and new application area in various fields of life. In this work, efforts have been made on the description of mathematical modeling of steady-state analysis of mediated amperometric system. Keywords: Mathematical modeling, conducting polymer, flux Introduction Computer stimulation is ‘experiment’ using reaction takes place, problems in differential calculus computer to realize meaningful result. It is less costly, will often be encountered. The purpose of the solution less time consuming and much safer than actual of these differential equation systems will be to provide physical experiment. Simulation is done in two steps. a description of the behavior of the system in a more The first step is to build reliable model. Then simulation manageable. Frequently algebraic form, predictive is performed as the second step with carefully studies and experimental data analysis can be readily chosen input and parameter. When the input and performed. Theoretical analysis will involve the parameter is not appropriate, model and simulation will relatively straightforward process of linking together give misleading and erroneous result. Simulation helps the different components of the system rather than in selecting suitable input set and design parameter starting completely afresh [2]. [1]. The advantage of using electrochemically Enzymes are biological catalysts and in the deposited polymers is their ease of preparation and presence of these enzymes biological reaction gets the uniformity of the prepared films. accelerated. These are the specialized group of proteins Provision of a formal theoretical description relies having specific three dimensional active structure and upon the available mathematical tools. Since, in active sites. An enzyme remains active at optimum considering biosensors, a chemical change will condition of temperature, pH, substrate concentration, generally be involved. This will most commonly be and enzyme concentration, inhibitors etc. These are based upon differential calculus, the mathematics of various parameters, which are used to measure the change. Further, with parameters changing both with rate of enzyme reaction, which involves substrate, time and with distance from the surface at which the which get converted into product with the help of çÚUâ¿ü °ÙæçÜçââ °‡ÇU §ßñËØé°àæÙ 127
  • 2. International Research Journal ISSN-0975-3486 VOL. I * ISSUE—3 &4 RNI : RAJBIL/2009/30097 enzyme. Therefore, the rate of reaction can be measured can be used for the immobilization of enzyme on an or determined by either measuring the rate at which inert electrode. The simplification of this system allows substrate is consumed or at the rate at which the us to set all fluxes as equal. This flux must also equate product is formed [3]. with the current for generation of the oxidized mediator The specific recognition characteristics of enzyme at the electrode. By varying substrate concentration antibodies and general receptor systems are employed (S∞), we have observed the changes in the observed to perform a variety of functions within the organisms flux (1/jobs). The characteristics of the observed flux from which they are isolated, catalysis, defence, and the interference effects on its performance have communication and control being the primary ones. been predicted. This specific recognition is based upon chemical Model Building binding of the one component to its complementary Researchers and engineers are usually develops partner, this being the target analyte and the biological physical models called ‘Scale model’. An amperometric component of the biosensor respectively. This enzyme substrate electrode with a PO2 basic sensor chemical binding can be very strong indeed and the [7], modeling and simulation of a diffusion limited binding process is frequently very rapid. Whatever glucose biosensor [8], a coupled two-compartment the normal function of a biological component within model for immobilized enzyme electrodes, an organism, the basic principle behind its capacity electrochemical immobilization of enzymes [9], for for specific recognition will be the same and, for our instance is build to study the measuring range, current purpose, we need concern ourselves only with sensitivity and response time of the sensor. Likewise, the fundamentals of the binding process as it relates amperometric enzyme electrodes [10], electrochemical to biosensors [4]. immobilization of enzyme electrodes [11] is built by Immobilized enzymes are used in many researchers and engineers. While these are useful, they applications both in synthetic and in analytical are, in most cases, static models. We are often interested chemistry [5]. Since, the works of Clark and Lyons, in the dynamic performance of system, before building hundreds of paper have been published regarding the the actual prototype. The physical models are difficult design of practical amperometric enzyme electrodes to build and can be expensive. for the analysis of clinically important metabolites and Most of the models can be structured as three- industrial monitoring. Among these reports, two kinds part system. Some input (substrate) is provided, of problems are always the main subject. One is the process (enzyme kinetics and chemical reaction) is done immobilization of enzyme. Different immobilization and we get some small output (small signal current). methods and materials have been developed including Consider the case of the mediated amperometric device. adsorption, cross-linking, self assembly methods and This is an example of considerable interest in biosensor conducting or non-conducting polymers as well as research. In this type of model, input may be substrate different types of gels. The aim of all these efforts was (glucose) and mediator is oxygen. The process starts to obtain an easy handling method with cheap and by defining the various elementary steps involved and stable material, which can retain high biological activity their rates. The system consists of an electrode, which of the enzyme. However, a good biosensor depends monitor and provides the measurement signal. The not only on a good immobilization method but also on electrolyte layer, which contains the mediator and the a sensitive tranducer. This is the other focus in the enzyme, an outer membrane which serves to control development of amperometric enzyme electrode [6]. diffusional mass transport to the electrolyte layer as In the present research work, efforts have been well as to physically constrain the electrolyte close to made on the description of mathematical modeling of the sensing electrode. steady-state analysis of mediated amperometric The steady state analysis of the mediated system. This model is presented for electrochemically- amperometric system illustrating the various transport polymerized thin films of conducting polymers which and kinetic processes is shown in Fig.1. Here, the 128
  • 3. International Research Journal ISSN-0975-3486 VOL. I * ISSUE—3&4 RNI : RAJBIL/2009/30097 substrate (S) and oxidized form of the enzyme (EO) Mathematical Structure reacts with each other and we get enzyme substrate Models are built with inter-related set of equations. complex (EOS). The next step is that this complex (EOS) These equations may be algebric or differential gives the product (P) and reduced form of the enzyme equations and with logical statements for constraints (ER). By allowing a particular rate of O2, we get, oxidized and bounds. Consider the case of steady-state analysis form of enzyme (EO) and reduced form of mediator (MR) of mediated amperometric system. It is a probabilistic and at the end at the electrode, reduced form of the model. By straightforward algebric manipulation, an mediator gets converted into oxidized form by releasing expression describing the output signal in terms of the 2e- (electrons). This gives the current at the electrode. various kinetic parameters characterizing the system All these reactions have particular rate. These rate can be derived and the substrate concentration, which constants are known as enzyme kinetics rate it is the purpose of the device to measure. The reaction constants. They are governed by Michaelis-Menten sequence upon which the system is based can be constant (KM). written as follows. Figure 1 Steady-state analysis of mediated The relation 1 and 2 represents the oxidation of amperometric system. substrate to product, according to Michaels-Menten To begin with models, they are built with a few kinetics by the oxidized (EO) enzyme to give the reduced algebraic equations and a few variables. They may form of the enzyme (ER). The relation 3 represents the provide a general description of the system. The reoxidation of the reduced enzyme by oxidized mediator mathematical model for conducting polymer based (MO), giving rise to the reduced mediator (MR). The amperometric sensor can built on the basis of material relation 4 represents the reoxidation of the mediator at used for the electrode, enzyme used, method of an electrode which gives rise to the current upon which immobilization used, conducting polymer used, size of the measurement is based. Rates of formation and the sensor which material it sense and what are its area disappearance of EoS-complex can be written as, of applications. More complex models would include the more than one enzyme immobilized, rate of electron transfer, rates of various enzyme kinetic reactions and environmental conditions etc. One of the major Where, Vf is the rate of formation and Vd is the decisions of a model builder is, then, to choose the rate of disappearance of the bimolecular EoS-complex. variables to be included in the model and to exclude The steady state assumptions “more complex” or less important variables. A model Consider homogeneous solution enzyme kinetics. can grow with addition of variables based on A steady state is established in which the rates of interactions with the users. different steps occurring in the electrolyte layer are çÚUâ¿ü °ÙæçÜçââ °‡ÇU §ßñËØé°àæÙ 129
  • 4. International Research Journal ISSN-0975-3486 VOL. I * ISSUE—3 &4 RNI : RAJBIL/2009/30097 balanced with one another and with the mass transport different dependence upon the three concentration of reactant and product to and from it. The assumption variables at our control, that of the substrate, enzyme requires that the sensing reaction cause negligible and mediator (O2). To test the model experimentally, change in the bulk solution concentrations of reactant we keep two of these concentrations (enzyme and and product. The approximation is valid, provided mediator) constant change the third and investigate that the electrolyte layer sufficiently thin so that the effects on the observed flux. Then, by taking diffusion times across it are short and that the diffusion double reciprocal plots and measuring slopes and rates are relatively rapid as compared with the enzyme intercepts from them, we can predict results of reaction rates. We assume that there is an excess of simulation about the characteristic rate for each step. mediator and that the electrode generates M0 from MR When the conducting polymer film is sufficiently thin sufficiently rapidly that the concentration of M0 is and there is no concentration polarization of either effectively that of the total mediator [M]. This enzyme (S) or oxygen (O2) within the film, then in steady condition can be arranged in practice by ensuring that state we can write, the reoxidation occurs rapidly at the electrode, the electrolyte layer is thin so that the diffusional mass transport of mediator across it to the electrode is also rapid and the mediator concentration is sufficiently in excess of the enzyme concentration. Estimation of flux of the substrate Using steady sate assumptions, a rate equation for the intermediate can be written as, d[EoS] /dt = k1[E][S] – k-1[EoS] – k2[EoS] = 0 [5] As the total concentration of enzyme [ET], at all times will be the sum of concentrations in free and complexed forms [E] + [EoS]. Now, putting [E] = [ET]- [EoS] in the above equation we get, d [EoS]/dt = k1[ET][S]– ( k1[S]+k–1+k2) [EoS] = 0 This equation represents the contribution to the [6] rate control by the reaction of reduced enzyme with the mediator to generate the oxidized enzyme. Equating equations 10 and 11 and solve them, we get, Putting this into the rate expression for At low substrate concentration, when the term (k decomposition of the complex to form the product KA a¥ KM) in the denominator is dominant, js µ S¥. As gives the rate (v) of product formation, the concentration of substrate is increased, either the v = k2[EoS] term (KA a¥ KS s¥) or the term (kcat KS S¥) becomes v = k2 [ET] [S]/ KM + [S] dominant and js becomes independent of the substrate concentration. This can occurs for two reasons. When the term (k KA a¥ KS s¥) is dominant, then js is limited by the saturated enzyme kinetics for the consumption of substrate. When the term (kcat KS S¥) is dominant, then In the above expression each term shows a js is limited by the rate of reoxidation of the enzyme by 130
  • 5. International Research Journal ISSN-0975-3486 VOL. I * ISSUE—3&4 RNI : RAJBIL/2009/30097 reaction with the mediator, under these circumstances the film, it is possible to estimate the kinetics of the js is depends on a¥. reactions of the immobilized enzyme. This is an Mathematical Model operational characteristic of value in a biosensor. By The flux of the substrate js reacting within the film varying the enzyme concentration [ET], membrane is not necessarily the same as the flux of reduced thickness and k D , one may investigate the mediator detected at the electrode jobs. This happens contributions of the rates of the two different steps to due to some of the mediator will be lost to the bulk the overall rate. In equation 16, each term shows a solution. The precise amount will depend on the different dependence upon the three concentration efficiency of mass transport of hydrogen peroxide variables at our control that of the substrate, enzyme (H2O2) away from the electrode. When this is very and mediator. efficient, then the concentration of hydrogen peroxide Conclusion (H2O2) held at zero. At the outside of the film, jobs = (js We have described the mathematical model of the / 2). It is assumed that, the experiment is carried out at steady state mechanism of amperometric system of the rotating disk electrode; the mass transport of electrochemically synthesized thin films of conducting hydrogen peroxide (H2O2) away from the electrode can polymer on which enzyme was assumed to be be controlled. We can show that, immobilized. The flux from which the measured signal jobs = (js / á) [13] obtained is directly proportional to substrate concentration. This is an operational characteristic of value in an enzyme electrode. One may use mathematical model for the development of conducting polymer based mediated amperometric system. R E F E R E N C E Note that, 1 < á < 2, as expected. By combining 1)“Computer based modeling and simulation 1. Modeling equations 12 and 14, we obtain the expression for the deterministic systems”, N.K. Srinivasan, Resonance, Journal observed current. of Science education, Volume 6. Number3, March-2001, 46- i = nFA js 54. 2) “Theoretical methods for analyzing biosensor Again, jobs = js á, we get, performance”, Mark. J. Eddowes 3) “Elements of biochemistry”, H.S. Srivastava. 4) “The organic chemistry of enzymes”, Richard B. Silverman, Academic press. 5) “Electrochemical immobilization of enzymes Part 1. Theory” P.N. Bartlett and R. G. Whitaker. J. Electronal Chem., 224, (1987), 27-35. 6) “Self-gelatinizable copolymer immobilized glucose biosensor based on Russian Blue modified Graphite electrode”, Qing Deng, Bin Li and Shaojun Dong. The Analyst, 1998, 123, 1995-1999, 1995. 7) “Mathematical simulation of an amperometric enzyme substrate electrode with a PO2 basic sensor. Part 1. Mathematical model and simulation of the PO2 basic sensor”, K. Lemke, Medical and Biological engineering and computing, Sept. 1988, 523-532. 8) “Modelling and Simulation of a diffusion limited glucose biosensor”, A.Cambioaso, L. Delfino at el. Sensors and Actuators, B33 (1996) 203- 207. 9) “Electrochemical Immobilization of enzymes.3: Immobilization of GOD in Thin films of Electrochemically Polymerized Phenols”, P.N. Bartlett, Peter Tebbutt and Claire H. Tyrrell, Anal. Chem., 64, (1992), 138- Now, by measuring the current for the enzyme 142. 10) “Amperometric enzyme electrodes: Theory and coated electrode as a function of the concentrations Experiments.The use of electrochemical methods in the study of modified electrodes”, P. N. Bartlett. of substrate, mediator and of the enzyme loading in çÚUâ¿ü °ÙæçÜçââ °‡ÇU §ßñËØé°àæÙ 131