<?xml version="1.0" encoding="UTF-8"?><!DOCTYPE article  PUBLIC "-//NLM//DTD Journal Publishing DTD v3.0 20080202//EN" "http://dtd.nlm.nih.gov/publishing/3.0/journalpublishing3.dtd"><article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" dtd-version="3.0" xml:lang="en" article-type="research article"><front><journal-meta><journal-id journal-id-type="publisher-id">NS</journal-id><journal-title-group><journal-title>Natural Science</journal-title></journal-title-group><issn pub-type="epub">2150-4091</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/ns.2013.53045</article-id><article-id pub-id-type="publisher-id">NS-29020</article-id><article-categories><subj-group subj-group-type="heading"><subject>Articles</subject></subj-group><subj-group subj-group-type="Discipline-v2"><subject>Biomedical&amp;Life Sciences</subject><subject> Chemistry&amp;Materials Science</subject><subject> Earth&amp;Environmental Sciences</subject><subject> Medicine&amp;Healthcare</subject><subject> Physics&amp;Mathematics</subject></subj-group></article-categories><title-group><article-title>
 
 
  Analytical expression of concentrations of adsorbed CO molecules, O atoms and oxide oxygen
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>hinnasamy</surname><given-names>Thangapandi</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Lakshmanan</surname><given-names>Rajendran</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib></contrib-group><aff id="aff1"><addr-line>Department of Mathematics, The Madura College, Madurai, India;</addr-line></aff><author-notes><corresp id="cor1">* E-mail:<email>raj_sms@rediffmail.com(LR)</email>;</corresp></author-notes><pub-date pub-type="epub"><day>26</day><month>03</month><year>2013</year></pub-date><volume>05</volume><issue>03</issue><fpage>326</fpage><lpage>332</lpage><history><date date-type="received"><day>12</day>	<month>October</month>	<year>2012</year></date><date date-type="rev-recd"><day>15</day>	<month>November</month>	<year>2012</year>	</date><date date-type="accepted"><day>27</day>	<month>November</month>	<year>2012</year></date></history><permissions><copyright-statement>&#169; Copyright  2014 by authors and Scientific Research Publishing Inc. </copyright-statement><copyright-year>2014</copyright-year><license><license-p>This work is licensed under the Creative Commons Attribution International License (CC BY). http://creativecommons.org/licenses/by/4.0/</license-p></license></permissions><abstract><p>
 
 
   A mathematical model of the oscillatory regimes of CO oxidation over plantinum-group metal catalysts are discussed. The model is based on nonstationary diffusion equation containing a nonlinear term related to Michaelis-Menten kinetics of the enzymatic reaction. This paper presents the analytical and numerical solution of the system of non-linear differential equations. Here the Homotopy perturbation method (HPM) is used to find out the analytical expressions of the concentration of CO molecules, O atom and oxide oxygen respectively. A comparison of the analytical approximation and numerical simulation is also presented. A good agreement between theoretical and numerical results is observed. 
 
</p></abstract><kwd-group><kwd>Oscillatory Dynamics; Reaction-Diffusion; Boundary Value Problems; Homotopy Perturbation Method</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. INTRODUCTION</title><p>Rate auto-oscillations in a heterogeneous catalytic reaction were first discussed more than two decades ago [1-3]. Some heterogeneous systems which show oscillatory behaviour on catalysts with various structures in a wide pressure range are presently known. One of the most extensively studied heterogeneous catalytic reactions exhibiting oscillatory dynamics is CO oxidation on platinum catalysts.</p><p>Various mathematical models are used in detailed analysis of the mechanism of the rate oscillations in catalytic CO oxidation. These models are based on a set of nonlinear ordinary differential equations [4-12]. Microscopic stochastic models by using the Monte Carlo method [13-18] one of the most interesting in theoretical investigation of the dynamics of fluctuating reaction systems. These stochastic models are based on detailed information concerning the elementary steps of the reaction, the structure of the catalyst surface, and the mobility of species in the adsorption layer.</p><p>Therefore, the theoretical investigation and explanation of complex dynamic phenomena on a catalyst surface cannot be comprehensive. It is necessary to develop systems of consistent mathematical models describing the evolution of reaction systems on different spatial scales. This would allow the advantages of different classes of mathematical models.</p><p>Recently Kurkina and Semendyaeva [<xref ref-type="bibr" rid="scirp.29020-ref3">3</xref>] described the oscillatory dynamical system which includes a Monte Carlo simulation and adsorption layer approximation. To our knowledge no analytical expressions of the concentration of CO molecules, O atom and oxide oxygen have been derived from the system. The purpose of the communication is to derive the analytical expression of<img src="2-8301827\9614d05a-8b39-4d6b-83e1-6ec3e1441494.jpg" />, <img src="2-8301827\947905f2-6d20-4b07-a76a-36a21ec60d0c.jpg" />, and <img src="2-8301827\d1a2ba9d-66ca-4a30-aee6-7c52a1b1acec.jpg" /> by solving the system of non-linear differential equation using Homotopy perturbation method.</p></sec><sec id="s2"><title>2. MATHEMATICAL FORMULATION OF BOUNDARY VALUE PROBLEM</title><p>The oscillatory dynamics of the thickness shear model (TSM) kinetic network will be described using Lattice gas model. In this model any lattice site may be free (*) or occupied by an adsorbed carbon monoxide molecule CO<sub>ads</sub>, an adsorbed oxygen atom O<sub>ads</sub> or an adsorbed oxide oxygen atom<img src="2-8301827\1ae9397d-5677-490b-ad10-677a37c60395.jpg" />. The thickness shear mode (TSM) kinetic network includes the Langmuir-Hinshelwood mechanism [<xref ref-type="bibr" rid="scirp.29020-ref3">3</xref>].</p><disp-formula id="scirp.29020-formula65475"><label>(1)</label><graphic position="anchor" xlink:href="2-8301827\2e12960a-db4a-441c-81dc-c1c1611a3555.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65476"><label>(2)</label><graphic position="anchor" xlink:href="2-8301827\300f6e9d-8969-406e-8210-5e3b818c3c86.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65477"><label>(3)</label><graphic position="anchor" xlink:href="2-8301827\fbd3d7fa-d6be-4bbb-8087-0d300db35a8c.jpg"  xlink:type="simple"/></disp-formula><p>and the formation and removal of surface oxide,</p><disp-formula id="scirp.29020-formula65478"><label>(4)</label><graphic position="anchor" xlink:href="2-8301827\9de0e56e-5987-41a6-ba5c-ba3390941e63.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65479"><label>(5)</label><graphic position="anchor" xlink:href="2-8301827\62dc69ba-6666-4c53-95e9-99e4e1fc1de9.jpg"  xlink:type="simple"/></disp-formula><p>Furthermore, we consider the migration of adsorbed species via a vacant-site mechanism:</p><disp-formula id="scirp.29020-formula65480"><label>(6)</label><graphic position="anchor" xlink:href="2-8301827\59c5cab0-9a50-431f-ac7e-2f035a34e24d.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65481"><label>(7)</label><graphic position="anchor" xlink:href="2-8301827\61a5888f-ed7d-4cb2-8547-f9acbe389848.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65482"><label>(8)</label><graphic position="anchor" xlink:href="2-8301827\c8a72f25-0852-47b3-b625-e7133ab15c05.jpg"  xlink:type="simple"/></disp-formula><p>Here, <img src="2-8301827\1eb01002-aac3-4dbe-93e8-c1ed6a1678cd.jpg" />and <img src="2-8301827\49add52c-b901-47be-9569-b9978e2e6bd4.jpg" /> are molecules in the gas phase. Two-site process occurs on adjacent lattice sites. The rate of a two-site process is defined for a pair of sites, and the rate of a one-site process is defined for one site. The surface oxide formation step (4) is viewed as a one-site process, and step (5) is a two-site process. It is assumed that oxide oxygen retains its reactivity (see step (5)) and markedly decreases the activity of the catalyst in reactant adsorption from the gas phase.</p></sec><sec id="s3"><title>3. STOCHASTIC AND DETERMINISTIC MODELS</title><p>The basic kinetic equations in a multidimensional system will be solved by approximate methods. In Monte Carlo stochastic modelling, state trajectories are constructed for the reaction system in the state space. Stochastic models describe the evolution of a selected lattice fragment at the atomic level. According to the above kinetic network, the variation of<img src="2-8301827\e51c3c16-0bb8-46d3-8237-c37dc58fb9c2.jpg" />, <img src="2-8301827\6530dfef-1ba7-4d2e-97d0-157af26d8f0d.jpg" />and <img src="2-8301827\786c8214-c637-49b4-a369-dfb2b44fa3ab.jpg" /> concentrations are described by a set of following nonlinear differential equations [<xref ref-type="bibr" rid="scirp.29020-ref4">4</xref>]:</p><disp-formula id="scirp.29020-formula65483"><label>(9)</label><graphic position="anchor" xlink:href="2-8301827\4a4c1c27-0c1b-445b-aab4-383c6624654d.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65484"><label>(10)</label><graphic position="anchor" xlink:href="2-8301827\965278b0-72ca-4ce6-b0d2-757838a350f0.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65485"><label>(11)</label><graphic position="anchor" xlink:href="2-8301827\71e15625-a80e-4dd0-b12c-a48f3533309e.jpg"  xlink:type="simple"/></disp-formula><p>The initial conditions are as follows:</p><disp-formula id="scirp.29020-formula65486"><label>(12)</label><graphic position="anchor" xlink:href="2-8301827\a2c97f2d-f2b6-4ee8-b4b8-080b65360c9d.jpg"  xlink:type="simple"/></disp-formula><p>Here, <img src="2-8301827\b9a2f878-e698-44e0-b667-0d720bacb607.jpg" />, <img src="2-8301827\2d0c5343-a17c-47ae-aeae-1edfb939636e.jpg" />, and <img src="2-8301827\9116d313-1844-438e-97d2-3a11d935a2bb.jpg" /> are the concentrations of adsorbed CO molecules and O atoms and oxide oxygen, respectively, and <img src="2-8301827\0b6237ad-e2bf-4718-bbf0-a89457578aa5.jpg" /> are the rate constants of elementary steps. The normalization conditions are as follows:</p><disp-formula id="scirp.29020-formula65487"><label>(13)</label><graphic position="anchor" xlink:href="2-8301827\4e9c7a8e-6411-4549-a9e4-2bdbff7bc478.jpg"  xlink:type="simple"/></disp-formula><p>To simplify, we can assume that<img src="2-8301827\eb1465bf-d468-4f6a-b616-5ca9e148fe09.jpg" />, <img src="2-8301827\8a679f9c-a4e1-42f0-8330-b386c615a3e8.jpg" />and <img src="2-8301827\378154cc-c201-4e12-90ee-90989fc70393.jpg" /> The above Eqs.9-11 become</p><disp-formula id="scirp.29020-formula65488"><label>(14)</label><graphic position="anchor" xlink:href="2-8301827\834e58b5-5ebb-427a-91fe-90da2e4fdf1b.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65489"><label>(15)</label><graphic position="anchor" xlink:href="2-8301827\b7f2827f-bc1b-4c7a-bc92-0561ca9ba81c.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65490"><label>(16)</label><graphic position="anchor" xlink:href="2-8301827\69a87525-aa44-467d-8c0b-9ded5e2977e9.jpg"  xlink:type="simple"/></disp-formula><p>Now the boundary condition (12) (or initial conditions) becomes</p><p><img src="2-8301827\6a9c9b9d-146a-4e68-ab4a-b4014463966c.jpg" /></p><p>where</p><disp-formula id="scirp.29020-formula65491"><label>(17)</label><graphic position="anchor" xlink:href="2-8301827\6fb3d64f-cd04-485a-b025-3ed79c18f2e2.jpg"  xlink:type="simple"/></disp-formula></sec><sec id="s4"><title>4. ANALYTICAL EXPRESSIONS OF CONCENTRATIONS USING HOMOTOPY PERTURBATION METHOD [HPM]</title><p>Recently, many authors have applied the HPM to various problems by demonstrating the efficiency of the HPM in handling non-linear structures and solving various physics and engineering problems [16-19]. This method is a combination in topology and classic perturbation techniques. Ji Huan He used the HPM to solve the light hill equation [<xref ref-type="bibr" rid="scirp.29020-ref20">20</xref>], the Duffing equation [<xref ref-type="bibr" rid="scirp.29020-ref21">21</xref>] and the Blasius equation [<xref ref-type="bibr" rid="scirp.29020-ref22">22</xref>]. The idea has been used to solve non-linear boundary value problems, integral equations and many other problems [23-27]. The HPM is unique in its applicability, accuracy and efficiency. The HPM uses the imbedding parameter p as a small parameter and only a few iterations are needed to search for an asymptotic solution. Using this method (see Appendix A), we can obtain the following solution to Eqs.14-16 for the given boundary conditions (Eq.17).</p><disp-formula id="scirp.29020-formula65492"><label>(18)</label><graphic position="anchor" xlink:href="2-8301827\72c7b9dc-3c45-4a2e-8214-9799948702b6.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65493"><label>(19)</label><graphic position="anchor" xlink:href="2-8301827\e1db130e-d620-46cc-b9e1-e71273874ff9.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65494"><label>(20)</label><graphic position="anchor" xlink:href="2-8301827\12830cf7-274d-4248-b1a0-407db8006b01.jpg"  xlink:type="simple"/></disp-formula><p>where</p><disp-formula id="scirp.29020-formula65495"><label>(21)</label><graphic position="anchor" xlink:href="2-8301827\bf7847d3-d52a-43f4-90d4-57c670b60bc5.jpg"  xlink:type="simple"/></disp-formula><p>The Eqs.18-20 represent the new closed form of analytical expression of concentrations of CO molecules, O atom and oxide oxygen for all values of rate constant and time.</p></sec><sec id="s5"><title>5. ANALYTICAL EXPRESSION OF CONCENTRATION FOR STEADY STATE CONDITION</title><p>For the case of steady state, the Eqs.14-16 become</p><disp-formula id="scirp.29020-formula65496"><label>(22)</label><graphic position="anchor" xlink:href="2-8301827\bf418e8b-bd6c-4ce9-8d30-4a6d8a7d4784.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65497"><label>(23)</label><graphic position="anchor" xlink:href="2-8301827\3ecb25a9-e2a0-4920-9f07-2f51c6b2054a.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65498"><label>(24)</label><graphic position="anchor" xlink:href="2-8301827\c526339a-f582-44d1-9aef-ef40a575260b.jpg"  xlink:type="simple"/></disp-formula><p>Solving the above non-linear algebraic equation by using Maple software, we can obtain the concentration of CO molecule, O atom and oxide oxygen as follows:</p><disp-formula id="scirp.29020-formula65499"><label>(25)</label><graphic position="anchor" xlink:href="2-8301827\24f38bdc-7b57-40a0-b3ad-9fc2cff246f8.jpg"  xlink:type="simple"/></disp-formula></sec><sec id="s6"><title>6. NUMERICAL SOLUTION</title><p>In order to test accuracy of this method the non-linear differential Eqs.14-16 for the boundary conditions (Eq.17) are solved by numerical methods. The function pdex4 in Matlab software was used to solve these equations. It is a function of solving the initial boundary value problems for non-linear differential equations. The Matlab program is also given in Appendix B. The numerical results are also compared with our analytical results in Figures 1(a)-(d). A satisfactory agreement is noted here.</p></sec><sec id="s7"><title>7. DISCUSSION</title><p>Figures 1(a)-(d) represent the non steady state concentration of CO molecules u(t) or<img src="2-8301827\3eac1eea-03b4-472b-ae4a-1ad1fc3d77c9.jpg" />, O atom v(t) or <img src="2-8301827\48d7b5b8-97ea-471d-b9dc-331023e68882.jpg" /> and oxide oxygen w(t) or <img src="2-8301827\50f00869-9ba8-4768-8a10-87511db9d216.jpg" /> for all values of rate constant and time. From the figure it is evident that the value of the concentration of CO molecule decrease from its initial value of concentration and reaches the steady state value zero when t = 2 sec for all values of rate constant. From the figures it is also inferred that the value of concentration of O atom rises initially and reaches the maximum value when t &#187; 0.5 sec and then decreases gradually. The concentration of O atom attains the steady state value when t = 10 sec. From this figure it is also observed that the concentration of oxide oxygen always increases when time increases and reaches the steady state value 1 when t = 5 sec for all values of rate constant. From this figure it is to conclude that <img src="2-8301827\6e6d3aed-c806-475d-a53e-3fb7205ee159.jpg" /> for all values of time and rate constant.</p></sec><sec id="s8"><title>8. CONCLUSION</title><p>The theory of the dynamics of catalysts CO oxidation in the frame work of the Thickness shear mode kinetic is described. Approximate analytical solutions to the system of non-linear reaction equations are presented using Homotopy perturbation method. A simple, straight forward and a new method of estimating the concentrations of CO molecules, O atom and Oxide oxygen are derived. This analytical result will be useful to know the behaviour of the reaction system. A good agreement with the numerical simulation data is also noted. The extension of</p><p>this method with more modelling and simulation procedure to the some of the non-linear reaction diffusion mechanism in biosensor [<xref ref-type="bibr" rid="scirp.29020-ref28">28</xref>] seems possible.</p></sec><sec id="s9"><title>9. ACKNOWLEDGEMENTS</title><p>This work is supported by the University Grants Commission (UGC) (Ref. No. F. No. 39 - 58/2010(SR)) and Council of Scientific and Industrial Research (CSIR) (No.01 (2442)/10/EMR-II), Government of India. The authors are thankful to the Secretary, the Principal, The Madura College, Madurai, India for their constant encouragement.</p></sec><sec id="s10"><title>REFERENCES</title></sec><sec id="s11"><title>APPENDIX A</title>Analytical Solution of the Nonlinear Equations Using Homotopy Perturbation Method<p>In this appendix, we indicate how Eqs.14-16 may be solved using HPM. To find the solution of Eqs.14-16, we first construct a homotopy as follows [16-19]:</p><disp-formula id="scirp.29020-formula65500"><label>(A1)</label><graphic position="anchor" xlink:href="2-8301827\a3d883d4-ba35-4afa-a419-8cf8c2f0e562.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65501"><label>(A2)</label><graphic position="anchor" xlink:href="2-8301827\29e688e3-52e5-4a9f-8b3e-4e245df248e6.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65502"><label>(A3)</label><graphic position="anchor" xlink:href="2-8301827\2e62c9b8-8770-4950-a945-2cea235bc975.jpg"  xlink:type="simple"/></disp-formula><p>where <img src="2-8301827\bdc0daa9-c7a4-4603-920f-a2101f563430.jpg" /> is an embedding parameter. According to HPM, we can first use the parameter p as a “small parameter” and assume that the solution of Eqs.14-16 can be written as a power series in p.</p><disp-formula id="scirp.29020-formula65503"><label>(A4)</label><graphic position="anchor" xlink:href="2-8301827\ef7e40ee-44ea-48c7-abe4-3081e7d95606.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65504"><label>(A5)</label><graphic position="anchor" xlink:href="2-8301827\c326fb53-8807-4d5a-8c35-e15cbea35c6d.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65505"><label>(A6)</label><graphic position="anchor" xlink:href="2-8301827\58ff9337-7710-458e-b59b-ca5870cf2271.jpg"  xlink:type="simple"/></disp-formula><p>where <img src="2-8301827\7d280fe9-47c5-4b34-94ae-ed2a3f8637d2.jpg" /> are zero-order solution (initial approximation) and <img src="2-8301827\0297b5ea-1098-49b6-ae08-9d0f54ca387e.jpg" /> are the first order approximate solution. When p = 0, we get zero-order solution (initial approximate solution or solution of linear terms). Setting p = 1, results in the approximate solution of Eqs.14-16. Substituting Eqs.A4-A6 into Eqs.A1-A3 and comparing the coefficients of like powers of p we obtain the following differential equations.</p><disp-formula id="scirp.29020-formula65506"><label>(A7)</label><graphic position="anchor" xlink:href="2-8301827\380eaebc-79db-468a-ae0d-d0c6254dad29.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65507"><label>(A8)</label><graphic position="anchor" xlink:href="2-8301827\072e0f6f-8b40-46eb-bf1d-dd4f46d60198.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65508"><label>(A9)</label><graphic position="anchor" xlink:href="2-8301827\36b999c5-120f-4f1a-96e8-315acb961861.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65509"><label>(A10)</label><graphic position="anchor" xlink:href="2-8301827\56e18dad-b06a-4bcc-afd3-51bef5f133e0.jpg"  xlink:type="simple"/></disp-formula><p>and</p><disp-formula id="scirp.29020-formula65510"><label>(A11)</label><graphic position="anchor" xlink:href="2-8301827\690c47e2-f3bc-415f-83dd-cf4a627c13c9.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65511"><label>(A12)</label><graphic position="anchor" xlink:href="2-8301827\168025d8-54b7-430e-997e-16b2a215e6ec.jpg"  xlink:type="simple"/></disp-formula><p>The initial conditions in Equation (17) becomes</p><disp-formula id="scirp.29020-formula65512"><label>(A13)</label><graphic position="anchor" xlink:href="2-8301827\c28c72f9-e4cc-459a-a055-b6bd385290f0.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65513"><label>(A14)</label><graphic position="anchor" xlink:href="2-8301827\e9e64fd3-30c3-44e2-9c02-3ce8d9f8246b.jpg"  xlink:type="simple"/></disp-formula><p>Solving the equations using the initial conditions Equation (A14), we obtain the following results.</p><disp-formula id="scirp.29020-formula65514"><label>(A15)</label><graphic position="anchor" xlink:href="2-8301827\7b4d0cc9-3124-4ce1-9116-16eeea0fc0f3.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65515"><label>(A16)</label><graphic position="anchor" xlink:href="2-8301827\e14cd6ed-3be8-4822-96d1-a21559d41c50.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65516"><label>(A17)</label><graphic position="anchor" xlink:href="2-8301827\309d07d9-457b-40ef-b9c3-73423f5300fa.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65517"><label>(A18)</label><graphic position="anchor" xlink:href="2-8301827\5d58f000-e292-4976-976f-2d23644e1960.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65518"><label>(A19)</label><graphic position="anchor" xlink:href="2-8301827\406ed4ae-67bf-4adc-b76f-f70dd2375ffd.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65519"><label>(A20)</label><graphic position="anchor" xlink:href="2-8301827\848e8cfa-4b98-4943-abbb-35195b37ccc6.jpg"  xlink:type="simple"/></disp-formula><p>According to the HPM, we can conclude that</p><disp-formula id="scirp.29020-formula65520"><label>(A21)</label><graphic position="anchor" xlink:href="2-8301827\78869d6a-daf2-4ed6-a86b-ca7dfd50f242.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65521"><label>(A22)</label><graphic position="anchor" xlink:href="2-8301827\93e913db-2a6c-4e87-98ea-2c65700a11d5.jpg"  xlink:type="simple"/></disp-formula><disp-formula id="scirp.29020-formula65522"><label>(A23)</label><graphic position="anchor" xlink:href="2-8301827\8f59f851-c842-4c52-8e0e-af0750c15ed5.jpg"  xlink:type="simple"/></disp-formula><p>where</p><disp-formula id="scirp.29020-formula65523"><label>(A24)</label><graphic position="anchor" xlink:href="2-8301827\4f5dae6d-8756-4680-82f9-6ef85564fe47.jpg"  xlink:type="simple"/></disp-formula><p>After putting the Eqs.A15-A20 in the Eqs.A21-A24 we get the Eqs.18-20 in the text.</p></sec><sec id="s12"><title>APPENDIX B</title>Matlab Program to Find the Numerical Solution of Eqs.14-16<p>function main1 options = odeset ('RelTol',1e-6,'Stats','on');</p><p>%initial conditions T=100;</p><p>Xo = [0.1; 0.5; 0.01];</p><p>tspan = [0,10];</p><p>tic</p><p>[t,X] = ode45(@TestFunction,tspan,Xo,options);</p><p>toc figure hold on plot(t, X(:,1))</p><p>plot(t, X(:,2))</p><p>plot(t, X(:,3),'.')</p><p>legend('x1','x2','x3')</p><p>ylabel('x')</p><p>xlabel('t')</p><p>return function [dx_dt]= TestFunction(t,x)</p><p>a=0.9,b=0.002,k2=0.5,k4=0.03,k5=0.2,k3=1,c=0.1,d=0.01,O=0.5dx_dt(1) =a*(1-x(1)-x(2)-x(3))-b*x(1)-4*k3*x(1)*x(2)-4*k5*x(1)*x(3);</p><p>dx_dt(2) =4*k2*(1-x(1)-x(2)-x(3))^2-4*k3*x(1)*x(2)-k4*x(2);</p><p>dx_dt(3)=k4*x(2)-4*k5*x(1)*x(3);</p><p>dx_dt = dx_dt';</p><p>return</p></sec></body><back><ref-list><title>References</title><ref id="scirp.29020-ref1"><label>1</label><mixed-citation publication-type="other" xlink:type="simple">Hugo, P. and Jakubith, M. 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