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<front>
<journal-meta>
<journal-id journal-id-type="pmc">FHMT</journal-id>
<journal-id journal-id-type="nlm-ta">FHMT</journal-id>
<journal-id journal-id-type="publisher-id">FHMT</journal-id>
<journal-title-group>
<journal-title>Frontiers in Heat and Mass Transfer</journal-title>
</journal-title-group>
<issn pub-type="epub">2151-8629</issn>
<publisher>
<publisher-name>Tech Science Press</publisher-name>
<publisher-loc>USA</publisher-loc>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">44587</article-id>
<article-id pub-id-type="doi">10.32604/fhmt.2023.044587</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Article</subject>
</subj-group>
</article-categories>
<title-group>
<article-title>Thermal Radiation Effects on 2D Stagnation Point Flow of a Heated Stretchable Sheet with Variable Viscosity and MHD in a Porous Medium</article-title>
<alt-title alt-title-type="left-running-head">Thermal Radiation Effects on 2D Stagnation Point Flow of a Heated Stretchable Sheet with Variable Viscosity and MHD in a Porous Medium</alt-title>
<alt-title alt-title-type="right-running-head">Thermal Radiation Effects on 2D Stagnation Point Flow of a Heated Stretchable Sheet with Variable Viscosity and MHD in a Porous Medium</alt-title>
</title-group>
<contrib-group>
<contrib id="author-1" contrib-type="author" corresp="yes">
<name name-style="western"><surname>Rehman</surname><given-names>Muhammad Abaid Ur</given-names></name><xref ref-type="aff" rid="aff-1">1</xref><email>abaidurrehman803@gmail.com</email></contrib>
<contrib id="author-2" contrib-type="author">
<name name-style="western"><surname>Farooq</surname><given-names>Muhammad Asif</given-names></name><xref ref-type="aff" rid="aff-1">1</xref></contrib>
<contrib id="author-3" contrib-type="author">
<name name-style="western"><surname>Hassan</surname><given-names>Ahmed M.</given-names></name><xref ref-type="aff" rid="aff-2">2</xref></contrib>
<aff id="aff-1"><label>1</label><institution>Department of Mathematics, School of Natural Sciences (SNS), National University of Sciences and Technology (NUST)</institution>, <addr-line>Sector H-12, Islamabad, 44000</addr-line>, <country>Pakistan</country></aff>
<aff id="aff-2"><label>2</label><institution>Faculty of Engineering, Future University in Egypt</institution>, <addr-line>New Cario</addr-line>, <country>Egypt</country></aff>
</contrib-group>
<author-notes>
<corresp id="cor1"><label>&#x002A;</label>Corresponding Author: Muhammad Abaid Ur Rehman. Email: <email>abaidurrehman803@gmail.com</email></corresp>
</author-notes>
<pub-date date-type="collection" publication-format="electronic">
<year>2024</year></pub-date>
<pub-date date-type="pub" publication-format="electronic"><day>21</day>
<month>3</month>
<year>2024</year></pub-date>
<volume>22</volume>
<issue>1</issue>
<fpage>263</fpage>
<lpage>286</lpage>
<history>
<date date-type="received">
<day>03</day>
<month>8</month>
<year>2023</year>
</date>
<date date-type="accepted">
<day>18</day>
<month>9</month>
<year>2023</year>
</date>
</history>
<permissions>
<copyright-statement>&#x00A9; 2024 Rehman, Farooq and Hassan</copyright-statement>
<copyright-year>2024</copyright-year>
<copyright-holder>Rehman, Farooq and Hassan</copyright-holder>
<license xlink:href="https://creativecommons.org/licenses/by/4.0/">
<license-p>This work is licensed under a <ext-link ext-link-type="uri" xlink:type="simple" xlink:href="https://creativecommons.org/licenses/by/4.0/">Creative Commons Attribution 4.0 International License</ext-link>, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.</license-p>
</license>
</permissions>
<self-uri content-type="pdf" xlink:href="TSP_FHMT_44587.pdf"></self-uri>
<abstract>
<p>This paper proposes a mathematical modeling approach to examine the two-dimensional flow stagnates at <inline-formula id="ieqn-1"><mml:math id="mml-ieqn-1"><mml:mi>x</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:math></inline-formula> over a heated stretchable sheet in a porous medium influenced by nonlinear thermal radiation, variable viscosity, and MHD. This study&#x2019;s main purpose is to examine how thermal radiation and varying viscosity affect fluid flow motion. Additionally, we consider the convective boundary conditions and incorporate the gyrotactic microorganisms equation, which describes microorganism behavior in response to fluid flow. The partial differential equations (PDEs) that represent the conservation equations for mass, momentum, energy, and microorganisms are then converted into a system of coupled ordinary differential equations (ODEs) through the inclusion of nonsimilarity variables. Using MATLAB&#x2019;s built-in solver bvp4c, the resulting ODEs are numerically solved. The model&#x2019;s complexity is assessed by plotting two-dimensional graphics of the solution profiles at various physical parameter values. The physical parameters considered in this study include skin friction coefficient, local Nusselt number, local Sherwood number, and density of motile microorganisms. These parameters measure, respectively, the roughness of the sheet, the transformation rate of heat, the rate at which mass is transferred to it, and the rate at which microorganisms are transferred to it. Our study shows that, depending on the magnetic parameter M, the presence of a porous medium causes a significant increase in fluid velocity, ranging from about 25% to 45%. Furthermore, with an increase in the Prandtl number <inline-formula id="ieqn-2"><mml:math id="mml-ieqn-2"><mml:mi>P</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula>, we have seen a notable improvement of about 6% in fluid thermal conductivity. Additionally, our latest findings are in good agreement with published research for particular values. This study provides valuable insights into the behavior of fluid flow under various physical conditions and can be useful in designing and optimizing industrial processes.</p>
</abstract>
<kwd-group kwd-group-type="author">
<kwd>Stagnation point flow</kwd>
<kwd>variable viscosity</kwd>
<kwd>variable thermal properties</kwd>
<kwd>heat source/sink</kwd>
<kwd>nanofluid</kwd>
</kwd-group>
</article-meta>
</front>
<body>
<sec id="s1">
<label>1</label>
<title>Introduction</title>
<p>Due to its potential applications in a number of sectors, including nanofluidic devices, drug delivery, and biomedical engineering, the stagnation point flow of nanomaterials with natural convection and variable fluid properties is a developing field that has drawn more attention nowadays. The thermal and physical characteristics of the fluid, such as viscosity, density, and thermal conductivity, have a significant impact on how nanomaterials behave at stagnation points. This study intends to examine the hydrodynamic flow of nanomaterials at stagnation point <inline-formula id="ieqn-38"><mml:math id="mml-ieqn-38"><mml:mi>x</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:math></inline-formula> with natural convection and variable fluid characteristics. The results of this study could have important implications for the design of nanofluidic devices and other applications where the behavior of nanomaterials at stagnation points is critical. Choi et al. [<xref ref-type="bibr" rid="ref-1">1</xref>] investigated the results of incorporating nanoparticles into fluids to increase their thermal conductivity. A theoretical analysis of the behavior of a nanofluid flow over a vertical plate under the effect of natural convection was reported by Kuznetsov et al. [<xref ref-type="bibr" rid="ref-2">2</xref>]. In a non-Darcy porous medium saturated with a nanofluid, Shaw et al. [<xref ref-type="bibr" rid="ref-3">3</xref>] investigated dual solutions for homogeneous-heterogeneous reactions over an elastic sheet. Their research sheds light on the effects of various parameters, including chemical reaction and non-Darcy effects on the flow of the nanofluid.</p>
<p>Magnetohydrodynamics (MHD) is a field of physics and engineering that studies the dynamics of electrically conducting fluids in the presence of magnetic fields. In MHD fluid flow, the fluid is influenced by electromagnetic fields, which can lead to interesting and complex phenomena such as the generation of electric fields and currents, the formation of magnetic structures, and the suppression of turbulence. MHD fluid flow has many practical applications in engineering, such as in plasma confinement for nuclear fusion, in the design of electric generators, and in the study of space weather. Roberts [<xref ref-type="bibr" rid="ref-4">4</xref>] and Davidson [<xref ref-type="bibr" rid="ref-5">5</xref>] served as introductory texts on Magnetohydrodynamics (MHD), providing basic concepts, principles, and applications of MHD in various fields of science and engineering. Qamar et al. [<xref ref-type="bibr" rid="ref-6">6</xref>] investigated the influence of variable electromagnetohydrodynamic (EMHD) on the motion of fluid over a porous elastic sheet. A hybrid nanofluid&#x2019;s magnetohydrodynamic stagnation point flow was studied by Anuar et al. in [<xref ref-type="bibr" rid="ref-7">7</xref>], along with the associated ODEs that were numerically solved using dual solutions. Zainal et al. [<xref ref-type="bibr" rid="ref-8">8</xref>] provided numerical solution of non-axisymmetric Homann impinging flow of hybrid nanofluid. Nadeem et al. [<xref ref-type="bibr" rid="ref-9">9</xref>] numerically analyzed the impact of different parameters on heat transfer and skin friction coefficient in the two-dimensional stagnation point flow of nanofluid over a curved surface. For the Newtonian magnetohydrodynamic fluid flow across an unsteady stretched sheet with thermal radiation, variable heat flux, and variable viscosity/conductivity, Megahed et al. [<xref ref-type="bibr" rid="ref-10">10</xref>] employed a shooting approach to solve the ordinary differential equations. Ali et al. [<xref ref-type="bibr" rid="ref-11">11</xref>] developed a mathematical model of 2D stagnation point flow over incorporated Newtonian heating.</p>
<p>Modeling nonlinear thermal radiation in fluid flow involves the use of complex mathematical models and numerical methods to obtain accurate predictions of the temperature field. The nonlinearity can significantly affect the temperature distribution in the fluid and has important implications for heat transfer in various engineering applications. In their study, Bouslimi et al. [<xref ref-type="bibr" rid="ref-12">12</xref>] studied the Williamson fluid under the influence of thermal radiation and electromagnetic force flowing in a porous material. According to Bilal et al. [<xref ref-type="bibr" rid="ref-13">13</xref>] the effects of nonlinear thermal radiation on the Darcy-Forchheimer flow of a magnetohydrodynamic Williamson nanofluid with entropy optimization are examined. Mixed convection micropolar fluid flow in a porous material with a magnetic field and boundary condition of convective type by Patel et al. [<xref ref-type="bibr" rid="ref-14">14</xref>], used similarity transformations and the Homotopy analysis approach to solve the governing equations with non-linear thermal radiation. To investigate the combined impact of various parameters on the Eyring-Powell nanofluid under the influence of MHD flow of through an elastic sheet, Reddy et al. [<xref ref-type="bibr" rid="ref-15">15</xref>] did an analysis. The findings were shown graphically and statistically. Kumar et al. [<xref ref-type="bibr" rid="ref-16">16</xref>] provided a detailed analysis of the Casson nanofluid in a vertical channel containing pores with the effect of MHD and thermal radiation.</p>
<p>The concept of the porous medium has gained significant attention in nowadays due to its numerous applications in scientific fields. A porous medium refers to a material with interconnected voids or spaces that allow fluid to pass through it. The presence of porous media in fluid flow systems often results in changes to the fluid&#x2019;s physical properties, including its viscosity. Understanding the impact of porous media on viscosity is crucial in designing and optimizing fluid flow systems for various applications. In this research paper, we aim to investigate the effects of porous media on fluid viscosity and explore its implications in practical applications. McWhirter et al. [<xref ref-type="bibr" rid="ref-17">17</xref>] presented experimental findings on magnetohydrodynamic flows in porous media, and shed light on the interaction between fluid flow, magnetic fields, and porous media. A mathematical model was developed by Bhatti et al. [<xref ref-type="bibr" rid="ref-18">18</xref>] for electromagnetic blood flow with coagulation, magnetohydrodynamics, and Hall current in an annular vessel with a porous medium, solved analytically for fluid and particle phase with the homotopy perturbation method. Reddy et al. [<xref ref-type="bibr" rid="ref-19">19</xref>] investigated the effect of MHD flow over a porous medium, obtained numerical solutions using the Keller-box method, and identified the flow features and their behavior under different parameters.</p>
<p>Bioconvection is a process where microorganisms are introduced into a fluid, causing the upper surface to become thicker and unstable, leading to the tumbling of microorganisms toward the ground. This process has numerous applications in various fields, such as pharmaceuticals, culture purification, microfluidics, mass transfer enhancement, oil recovery, and enzyme biosensors, and is currently a subject of ongoing research [<xref ref-type="bibr" rid="ref-20">20</xref>]. The flow of nanofluids comprising nanomaterials and motile microorganisms through a porous elastic wedge with Nield boundary through a porous matrix was the subject of research by Hussain et al. [<xref ref-type="bibr" rid="ref-21">21</xref>]. Muhammad et al. [<xref ref-type="bibr" rid="ref-22">22</xref>] examined the effects of activation energy, magnetic field, and other physical variables, as well as motile microorganisms, on the characteristics of Jeffrey nanofluid flow on a three-dimensional surface. Numerical analysis of a nanofluid flow via an elastic surface containing gyrotactic microorganisms was performed by [<xref ref-type="bibr" rid="ref-23">23</xref>&#x2013;<xref ref-type="bibr" rid="ref-25">25</xref>]. The study by Dawar et al. [<xref ref-type="bibr" rid="ref-26">26</xref>] compared the results of magnetized and non-magnetized Casson fluids through a stretching cylinder.</p>
<p>The research questions and innovatives explored in this research are as follows:
<list list-type="bullet">
<list-item>
<p>How does the viscoelastic parameter <italic>K</italic> influence the flow characteristics and boundary layer behavior of the fluid near the heated sheet?</p></list-item>
<list-item>
<p>How does the magnetic parameter <italic>M</italic> influence fluid velocity and transfer rate of heat?</p></list-item>
<list-item>
<p>What is the relationship between the bioconvection Lewis number <inline-formula id="ieqn-39"><mml:math id="mml-ieqn-39"><mml:mi>L</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula> and the density number in the context of bioconvection phenomena?</p></list-item>
</list></p>
<p>In the literature, the effects of gyrotactic microorganisms in two dimensional <inline-formula id="ieqn-40"><mml:math id="mml-ieqn-40"><mml:mo stretchy="false">(</mml:mo><mml:mn>2</mml:mn><mml:mi>D</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula> flow stagnates at <inline-formula id="ieqn-41"><mml:math id="mml-ieqn-41"><mml:mi>x</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:math></inline-formula> over an extended stretchable surface are limited. In this study, these effects for two-dimensional stagnation point flow [<xref ref-type="bibr" rid="ref-11">11</xref>] at <inline-formula id="ieqn-42"><mml:math id="mml-ieqn-42"><mml:mi>x</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:math></inline-formula> over an extended heated stretchable sheet are being investigated by considering factors such as nonlinear thermal radiation, MHD, porous medium, and variable viscosity. The governing PDEs will be transformed into ODEs using a similarity transformation and then numerically tackled using the <italic>bvp4c</italic> method in MATLAB [<xref ref-type="bibr" rid="ref-27">27</xref>&#x2013;<xref ref-type="bibr" rid="ref-31">31</xref>]. The resulting solutions will be plotted in two-dimensional graphics to illustrate the models&#x2019; complexity at various fluid parameter values.</p>
<p>The paper is structured into several sections, starting with the mathematical model of the problem in the <xref ref-type="sec" rid="s2">Section 2</xref>, followed by a discussion of the numerical approach in the <xref ref-type="sec" rid="s3">Section 3</xref>. The <xref ref-type="sec" rid="s4">Section 4</xref> presents the findings and a conclusion is drawn in the <xref ref-type="sec" rid="s5">Section 5</xref>.</p>
</sec>
<sec id="s2">
<label>2</label>
<title>Mathematical Modeling</title>
<p>Consider a two-dimensional viscoelastic nano-fluid flow stagnates at <inline-formula id="ieqn-43"><mml:math id="mml-ieqn-43"><mml:mi>x</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:math></inline-formula> containing gyrotactic microorganisms across an heated elastic sheet, taking into account that magnetic field applied vertical in direction to the surface, as well as Joule heating and viscous dissipation. At the stagnation point <inline-formula id="ieqn-44"><mml:math id="mml-ieqn-44"><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula>, two equal and opposing forces stretching the surface with velocities <inline-formula id="ieqn-45"><mml:math id="mml-ieqn-45"><mml:msub><mml:mi>u</mml:mi><mml:mi>w</mml:mi></mml:msub><mml:mo>=</mml:mo><mml:mi>a</mml:mi><mml:mi>x</mml:mi></mml:math></inline-formula> and <inline-formula id="ieqn-46"><mml:math id="mml-ieqn-46"><mml:msub><mml:mi>u</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub><mml:mo>=</mml:mo><mml:mi>b</mml:mi><mml:mi>x</mml:mi></mml:math></inline-formula>. To ignore the impact of the induced magnetic field, the magnetic Reynolds number must be very low. The momentum equation has the following form after the boundary layer approximation [<xref ref-type="bibr" rid="ref-11">11</xref>].</p>
<p><disp-formula id="eqn-1"><label>(1)</label><mml:math id="mml-eqn-1" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:mfrac><mml:mrow><mml:mi mathvariant="normal">&#x2202;</mml:mi><mml:mi>u</mml:mi></mml:mrow><mml:mrow><mml:mi mathvariant="normal">&#x2202;</mml:mi><mml:mi>x</mml:mi></mml:mrow></mml:mfrac><mml:mo>+</mml:mo><mml:mfrac><mml:mrow><mml:mi mathvariant="normal">&#x2202;</mml:mi><mml:mi>v</mml:mi></mml:mrow><mml:mrow><mml:mi mathvariant="normal">&#x2202;</mml:mi><mml:mi>y</mml:mi></mml:mrow></mml:mfrac><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p><disp-formula id="eqn-2"><label>(2)</label><mml:math id="mml-eqn-2" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:mi>u</mml:mi><mml:msub><mml:mi>u</mml:mi><mml:mi>x</mml:mi></mml:msub><mml:mo>+</mml:mo><mml:mi>v</mml:mi><mml:msub><mml:mi>v</mml:mi><mml:mi>y</mml:mi></mml:msub></mml:mtd><mml:mtd><mml:mi></mml:mi><mml:mo>=</mml:mo><mml:mspace width="thinmathspace" /><mml:msub><mml:mi>u</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:msub><mml:mi>u</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mo stretchy="false">)</mml:mo><mml:mi>x</mml:mi></mml:msub><mml:mo>&#x2212;</mml:mo><mml:mfrac><mml:mrow><mml:msub><mml:mi>&#x03C3;</mml:mi><mml:mi>e</mml:mi></mml:msub><mml:msubsup><mml:mi>B</mml:mi><mml:mn>0</mml:mn><mml:mn>2</mml:mn></mml:msubsup><mml:mo stretchy="false">(</mml:mo><mml:mi>u</mml:mi><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>u</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow></mml:msub><mml:mo stretchy="false">)</mml:mo></mml:mrow><mml:msub><mml:mi>&#x03C1;</mml:mi><mml:mi>f</mml:mi></mml:msub></mml:mfrac><mml:mo>+</mml:mo><mml:mfrac><mml:mn>1</mml:mn><mml:msub><mml:mi>&#x03C1;</mml:mi><mml:mi>f</mml:mi></mml:msub></mml:mfrac><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03BC;</mml:mi><mml:msub><mml:mi>u</mml:mi><mml:mi>y</mml:mi></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mi>y</mml:mi></mml:msub><mml:mo>&#x2212;</mml:mo><mml:mfrac><mml:mi>&#x03BC;</mml:mi><mml:mrow><mml:msub><mml:mi>&#x03C1;</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:mi>k</mml:mi></mml:mrow></mml:mfrac><mml:mrow><mml:mo>(</mml:mo><mml:mi>u</mml:mi><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>u</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mi></mml:mi><mml:mspace width="1em" /><mml:mo>+</mml:mo><mml:msub><mml:mi>k</mml:mi><mml:mn>0</mml:mn></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>u</mml:mi><mml:msub><mml:mi>u</mml:mi><mml:mrow><mml:mi>x</mml:mi><mml:mi>y</mml:mi><mml:mi>y</mml:mi></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:msub><mml:mi>u</mml:mi><mml:mi>x</mml:mi></mml:msub><mml:msub><mml:mi>u</mml:mi><mml:mrow><mml:mi>y</mml:mi><mml:mi>y</mml:mi></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:mi>&#x03BD;</mml:mi><mml:msub><mml:mi>u</mml:mi><mml:mrow><mml:mi>x</mml:mi><mml:mi>x</mml:mi><mml:mi>x</mml:mi></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>u</mml:mi><mml:mi>y</mml:mi></mml:msub><mml:msub><mml:mi>u</mml:mi><mml:mrow><mml:mi>x</mml:mi><mml:mi>y</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>and the corresponding boundary conditions are</p>
<p><disp-formula id="eqn-3"><label>(3)</label><mml:math id="mml-eqn-3" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd /><mml:mtd><mml:mi>u</mml:mi><mml:mo>=</mml:mo><mml:msub><mml:mi>u</mml:mi><mml:mi>w</mml:mi></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mi>x</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mi>a</mml:mi><mml:mi>x</mml:mi><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>v</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>w</mml:mi><mml:mi>h</mml:mi><mml:mi>e</mml:mi><mml:mi>n</mml:mi><mml:mspace width="1em" /><mml:mi>y</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mi>u</mml:mi><mml:mo stretchy="false">&#x2192;</mml:mo><mml:mrow><mml:msub><mml:mi>u</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mi>x</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:mrow><mml:mo>=</mml:mo><mml:mi>b</mml:mi><mml:mi>x</mml:mi><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>w</mml:mi><mml:mi>h</mml:mi><mml:mi>e</mml:mi><mml:mi>n</mml:mi><mml:mspace width="1em" /><mml:mi>y</mml:mi><mml:mo stretchy="false">&#x2192;</mml:mo><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>where <inline-formula id="ieqn-47"><mml:math id="mml-ieqn-47"><mml:mo stretchy="false">(</mml:mo><mml:mi>u</mml:mi><mml:mo>,</mml:mo><mml:mi>v</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mo>,</mml:mo><mml:msub><mml:mi>u</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub><mml:mo>,</mml:mo><mml:msub><mml:mi>u</mml:mi><mml:mi>w</mml:mi></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mi>x</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mo>,</mml:mo><mml:msub><mml:mi>&#x03BD;</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mo>,</mml:mo><mml:msub><mml:mi>&#x03C3;</mml:mi><mml:mi>e</mml:mi></mml:msub><mml:mo>,</mml:mo><mml:msub><mml:mi>k</mml:mi><mml:mn>0</mml:mn></mml:msub><mml:mo>,</mml:mo></mml:math></inline-formula> and <inline-formula id="ieqn-48"><mml:math id="mml-ieqn-48"><mml:msub><mml:mi>&#x03C1;</mml:mi><mml:mi>f</mml:mi></mml:msub></mml:math></inline-formula> represent the fluid velocities, free stream velocity, velocity of the sheet, kinematic viscosity, electrical conductivity, viscoelastic parameter, and fluid density, respectively.</p>
<p>In <xref ref-type="disp-formula" rid="eqn-2">(2)</xref>, the fluid viscosity <inline-formula id="ieqn-49"><mml:math id="mml-ieqn-49"><mml:mi>&#x03BC;</mml:mi></mml:math></inline-formula> is assumed to vary with temperature as follows:</p>
<p><disp-formula id="eqn-4"><label>(4)</label><mml:math id="mml-eqn-4" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:mi>&#x03BC;</mml:mi><mml:mo>=</mml:mo><mml:msub><mml:mi>&#x03BC;</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow></mml:msub><mml:msup><mml:mi>e</mml:mi><mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mi>&#x03B1;</mml:mi><mml:mi>&#x03B8;</mml:mi></mml:mrow></mml:msup><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>A similarity transformation is employed as follows [<xref ref-type="bibr" rid="ref-11">11</xref>]:</p>
<p><disp-formula id="eqn-5"><label>(5)</label><mml:math id="mml-eqn-5" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:mi>&#x03B7;</mml:mi><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msqrt><mml:mfrac><mml:mi>a</mml:mi><mml:msub><mml:mi>&#x03BD;</mml:mi><mml:mi>f</mml:mi></mml:msub></mml:mfrac></mml:msqrt><mml:mspace width="1em" /><mml:mi>u</mml:mi><mml:mo>=</mml:mo><mml:mi>a</mml:mi><mml:mi>x</mml:mi><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mi>&#x03B7;</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>v</mml:mi><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msqrt><mml:mi>a</mml:mi><mml:msub><mml:mi>&#x03BD;</mml:mi><mml:mi>f</mml:mi></mml:msub></mml:msqrt><mml:mi>f</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mi>&#x03B7;</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>We get the following ODE with boundary conditions as</p>
<p><disp-formula id="eqn-6"><label>(6)</label><mml:math id="mml-eqn-6" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd /><mml:mtd><mml:mi>f</mml:mi><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2033;</mml:mo></mml:mrow></mml:msup><mml:mo>&#x2212;</mml:mo><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mo>+</mml:mo><mml:mi>K</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mn>2</mml:mn><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2033;</mml:mo></mml:mrow></mml:msup><mml:mo>&#x2212;</mml:mo><mml:mi>f</mml:mi><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2033;</mml:mo></mml:mrow></mml:msup><mml:mo>&#x2212;</mml:mo><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2033;</mml:mo><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mo>)</mml:mo></mml:mrow><mml:mo>+</mml:mo><mml:mrow><mml:mo>(</mml:mo><mml:mi>M</mml:mi><mml:mo>+</mml:mo><mml:msup><mml:mi>e</mml:mi><mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mi>&#x03B1;</mml:mi><mml:mi>&#x03B8;</mml:mi></mml:mrow></mml:msup><mml:mi>&#x03B4;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03BB;</mml:mi><mml:mo>&#x2212;</mml:mo><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo>)</mml:mo></mml:mrow><mml:mo>+</mml:mo><mml:msup><mml:mi>&#x03BB;</mml:mi><mml:mn>2</mml:mn></mml:msup></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mi></mml:mi><mml:mo>+</mml:mo><mml:msup><mml:mi>e</mml:mi><mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mi>&#x03B1;</mml:mi><mml:mi>&#x03B8;</mml:mi></mml:mrow></mml:msup><mml:mrow><mml:mo>(</mml:mo><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2034;</mml:mo></mml:mrow></mml:msup><mml:mo>&#x2212;</mml:mo><mml:mi>&#x03B1;</mml:mi><mml:msup><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2033;</mml:mo></mml:mrow></mml:msup><mml:mo>)</mml:mo></mml:mrow><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p><disp-formula id="eqn-7"><label>(7)</label><mml:math id="mml-eqn-7" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:mi>f</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mn>1</mml:mn><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mi mathvariant="normal">&#x221E;</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mi>&#x03BB;</mml:mi><mml:mo>.</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>Here, the viscoelastic parameter is defined as <inline-formula id="ieqn-50"><mml:math id="mml-ieqn-50"><mml:mi>K</mml:mi><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mi>a</mml:mi><mml:msub><mml:mi>k</mml:mi><mml:mn>0</mml:mn></mml:msub></mml:mrow><mml:msub><mml:mi>&#x03BD;</mml:mi><mml:mi>f</mml:mi></mml:msub></mml:mfrac></mml:mstyle></mml:math></inline-formula>, while the external magnetic source is represented by <inline-formula id="ieqn-51"><mml:math id="mml-ieqn-51"><mml:mi>M</mml:mi><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:msub><mml:mi>&#x03C3;</mml:mi><mml:mrow><mml:mi>e</mml:mi></mml:mrow></mml:msub><mml:msubsup><mml:mi>B</mml:mi><mml:mrow><mml:mn>0</mml:mn></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msubsup></mml:mrow><mml:mrow><mml:mi>a</mml:mi><mml:msub><mml:mi>&#x03C1;</mml:mi><mml:mi>f</mml:mi></mml:msub></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula>. Additionally, the local Darcy number is given by <inline-formula id="ieqn-52"><mml:math id="mml-ieqn-52"><mml:mi>&#x03B4;</mml:mi><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mi>&#x03BC;</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow></mml:msub><mml:mrow><mml:msub><mml:mi>&#x03C1;</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:mi>k</mml:mi><mml:mi>a</mml:mi></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula>, the viscosity parameter is defined as <inline-formula id="ieqn-53"><mml:math id="mml-ieqn-53"><mml:mi>&#x03B1;</mml:mi></mml:math></inline-formula>, the ratio parameter is denoted by <inline-formula id="ieqn-54"><mml:math id="mml-ieqn-54"><mml:mi>&#x03BB;</mml:mi><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mi>b</mml:mi><mml:mi>a</mml:mi></mml:mfrac></mml:mstyle></mml:math></inline-formula> denotes the ratio parameter and <inline-formula id="ieqn-55"><mml:math id="mml-ieqn-55"><mml:mi>&#x03B1;</mml:mi></mml:math></inline-formula> represents the dimensionless viscosity parameter.</p>
<sec id="s2_1">
<label>2.1</label>
<title>Energy Equation</title>
<p>The energy equation in fluids describes the conservation of energy in fluid flow, accounting for thermal energy transfer due to conduction, convection, and radiation. It is an important equation in fluid dynamics and is commonly used in the analysis of heat transfer problems. After boundary layer approximation, the energy equation [<xref ref-type="bibr" rid="ref-11">11</xref>] takes the following form:</p>
<p><disp-formula id="eqn-8"><label>(8)</label><mml:math id="mml-eqn-8" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:mi>u</mml:mi><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi>x</mml:mi></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:mi>v</mml:mi><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi>y</mml:mi></mml:mrow></mml:msub></mml:mtd><mml:mtd><mml:mi></mml:mi><mml:mo>=</mml:mo><mml:mfrac><mml:msub><mml:mi>&#x03BC;</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mrow><mml:msub><mml:mi>&#x03C1;</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>c</mml:mi><mml:mi>p</mml:mi></mml:msub></mml:mrow></mml:mfrac><mml:msup><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>u</mml:mi><mml:mi>y</mml:mi></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mn>2</mml:mn></mml:msup><mml:mo>&#x2212;</mml:mo><mml:mfrac><mml:mrow><mml:msub><mml:mi>&#x03C3;</mml:mi><mml:mi>e</mml:mi></mml:msub><mml:msubsup><mml:mi>B</mml:mi><mml:mn>0</mml:mn><mml:mn>2</mml:mn></mml:msubsup><mml:mo stretchy="false">(</mml:mo><mml:mi>u</mml:mi><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>u</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow></mml:msub><mml:mo stretchy="false">)</mml:mo></mml:mrow><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C1;</mml:mi><mml:mi>c</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac><mml:mo>+</mml:mo><mml:mi>&#x03C4;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>D</mml:mi><mml:mrow><mml:mi>B</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi>y</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>C</mml:mi><mml:mrow><mml:mi>y</mml:mi></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:mfrac><mml:msub><mml:mi>D</mml:mi><mml:mi>T</mml:mi></mml:msub><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow></mml:msub></mml:mfrac><mml:msup><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi>y</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mn>2</mml:mn></mml:msup><mml:mo>)</mml:mo></mml:mrow></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mi></mml:mi><mml:mspace width="1em" /><mml:mo>&#x2212;</mml:mo><mml:mfrac><mml:mrow><mml:msub><mml:mi>Q</mml:mi><mml:mrow><mml:mn>0</mml:mn></mml:mrow></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>T</mml:mi><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:mrow><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C1;</mml:mi><mml:msub><mml:mi>c</mml:mi><mml:mrow><mml:mi>p</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac><mml:mo>+</mml:mo><mml:mfrac><mml:mn>1</mml:mn><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C1;</mml:mi><mml:mi>c</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>K</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mi>T</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mi>T</mml:mi><mml:mrow><mml:mi>y</mml:mi></mml:mrow><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mi>y</mml:mi></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>and the corresponding boundary conditions are</p>
<p><disp-formula id="eqn-9"><label>(9)</label><mml:math id="mml-eqn-9" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:mo>&#x2212;</mml:mo><mml:mi>K</mml:mi><mml:mfrac><mml:mrow><mml:mi mathvariant="normal">&#x2202;</mml:mi><mml:mi>T</mml:mi></mml:mrow><mml:mrow><mml:mi mathvariant="normal">&#x2202;</mml:mi><mml:mi>y</mml:mi></mml:mrow></mml:mfrac></mml:mtd><mml:mtd><mml:mi></mml:mi><mml:mo>=</mml:mo><mml:mo stretchy="false">[</mml:mo><mml:mi>T</mml:mi><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>T</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mo stretchy="false">]</mml:mo><mml:msub><mml:mi>h</mml:mi><mml:mrow><mml:mn>1</mml:mn></mml:mrow></mml:msub><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>w</mml:mi><mml:mi>h</mml:mi><mml:mi>e</mml:mi><mml:mi>n</mml:mi><mml:mspace width="1em" /><mml:mi>y</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mspace width="1em" /><mml:mi>T</mml:mi><mml:mo>=</mml:mo><mml:msub><mml:mi>T</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>w</mml:mi><mml:mi>h</mml:mi><mml:mi>e</mml:mi><mml:mi>n</mml:mi><mml:mspace width="1em" /><mml:mi>y</mml:mi><mml:mo stretchy="false">&#x2192;</mml:mo><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>where <inline-formula id="ieqn-56"><mml:math id="mml-ieqn-56"><mml:msub><mml:mi>T</mml:mi><mml:mi>f</mml:mi></mml:msub></mml:math></inline-formula> refers to the fluid&#x2019;s temperature, kinematic viscosity is represented by <inline-formula id="ieqn-57"><mml:math id="mml-ieqn-57"><mml:msub><mml:mi>&#x03BD;</mml:mi><mml:mi>f</mml:mi></mml:msub></mml:math></inline-formula>, <inline-formula id="ieqn-58"><mml:math id="mml-ieqn-58"><mml:msub><mml:mi>&#x03C3;</mml:mi><mml:mi>e</mml:mi></mml:msub></mml:math></inline-formula> represents the electrical conductivity, <inline-formula id="ieqn-59"><mml:math id="mml-ieqn-59"><mml:msub><mml:mi>&#x03C1;</mml:mi><mml:mi>f</mml:mi></mml:msub></mml:math></inline-formula> is the fluid&#x2019;s density, <inline-formula id="ieqn-60"><mml:math id="mml-ieqn-60"><mml:msub><mml:mi>Q</mml:mi><mml:mn>0</mml:mn></mml:msub></mml:math></inline-formula> is the heat source parameter, <inline-formula id="ieqn-61"><mml:math id="mml-ieqn-61"><mml:msub><mml:mi>D</mml:mi><mml:mi>B</mml:mi></mml:msub></mml:math></inline-formula> denotes brownian diffusion, <inline-formula id="ieqn-62"><mml:math id="mml-ieqn-62"><mml:msub><mml:mi>u</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub></mml:math></inline-formula> is the velocity of the free stream, <inline-formula id="ieqn-63"><mml:math id="mml-ieqn-63"><mml:msub><mml:mi>k</mml:mi><mml:mn>0</mml:mn></mml:msub></mml:math></inline-formula> refers to the viscoelastic parameter, and <inline-formula id="ieqn-64"><mml:math id="mml-ieqn-64"><mml:msub><mml:mi>B</mml:mi><mml:mn>0</mml:mn></mml:msub></mml:math></inline-formula> represents the magnetic parameter. In <xref ref-type="disp-formula" rid="eqn-8">(8)</xref>, the thermal conductivity <inline-formula id="ieqn-65"><mml:math id="mml-ieqn-65"><mml:mi>K</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mi>T</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula> is written as follows:</p>
<p><disp-formula id="eqn-10"><label>(10)</label><mml:math id="mml-eqn-10" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:mi>K</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mi>T</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:msub><mml:mi>K</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mn>1</mml:mn><mml:mo>+</mml:mo><mml:mi>&#x03B5;</mml:mi><mml:mi>&#x03B8;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>Using the following similarity transformation [<xref ref-type="bibr" rid="ref-11">11</xref>] in <xref ref-type="disp-formula" rid="eqn-8">Eq. (8)</xref>:</p>
<p><disp-formula id="eqn-11"><label>(11)</label><mml:math id="mml-eqn-11" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd /><mml:mtd><mml:mi>&#x03B7;</mml:mi><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msqrt><mml:mfrac><mml:mi>a</mml:mi><mml:msub><mml:mi>&#x03BD;</mml:mi><mml:mi>f</mml:mi></mml:msub></mml:mfrac></mml:msqrt><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>&#x03B8;</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mi>&#x03B7;</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mfrac><mml:mrow><mml:mi>T</mml:mi><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>T</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub></mml:mrow><mml:mrow><mml:msub><mml:mi>T</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow></mml:msub></mml:mrow></mml:mfrac><mml:mo>,</mml:mo></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mi>u</mml:mi><mml:mo>=</mml:mo><mml:mi>a</mml:mi><mml:mi>x</mml:mi><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>v</mml:mi><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msqrt><mml:mi>a</mml:mi><mml:msub><mml:mi>&#x03BD;</mml:mi><mml:mi>f</mml:mi></mml:msub></mml:msqrt><mml:mi>f</mml:mi><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>We get</p>
<p><disp-formula id="eqn-12"><label>(12)</label><mml:math id="mml-eqn-12" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:mo stretchy="false">(</mml:mo><mml:mn>1</mml:mn></mml:mtd><mml:mtd><mml:mi></mml:mi><mml:mo>+</mml:mo><mml:mi>&#x03B5;</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mi>&#x03B8;</mml:mi><mml:mo>+</mml:mo><mml:mi>&#x03B5;</mml:mi><mml:msup><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mo>+</mml:mo><mml:mi>P</mml:mi><mml:mi>r</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>f</mml:mi><mml:msup><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo>+</mml:mo><mml:mi>E</mml:mi><mml:mi>c</mml:mi><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2033;</mml:mo><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mo>+</mml:mo><mml:mi>M</mml:mi><mml:mi>E</mml:mi><mml:mi>c</mml:mi><mml:msup><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03BB;</mml:mi><mml:mo>&#x2212;</mml:mo><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mo>+</mml:mo><mml:mi>N</mml:mi><mml:mi>b</mml:mi><mml:msup><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:msup><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo>+</mml:mo><mml:mi>N</mml:mi><mml:mi>t</mml:mi><mml:msup><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mo>+</mml:mo><mml:mi>&#x03B3;</mml:mi><mml:mi>&#x03B8;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p><disp-formula id="eqn-13"><label>(13)</label><mml:math id="mml-eqn-13" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:msup><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mrow><mml:mn>1</mml:mn></mml:mrow></mml:msub><mml:mo stretchy="false">[</mml:mo><mml:mn>1</mml:mn><mml:mo>&#x2212;</mml:mo><mml:mi>&#x03B8;</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo stretchy="false">]</mml:mo><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>&#x03B8;</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mi mathvariant="normal">&#x221E;</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mn>0.</mml:mn></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>The ratio parameter is denoted by <inline-formula id="ieqn-66"><mml:math id="mml-ieqn-66"><mml:mi>&#x03BB;</mml:mi><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mi>b</mml:mi><mml:mi>a</mml:mi></mml:mfrac></mml:mstyle></mml:math></inline-formula>, which is equal to the ratio of <inline-formula id="ieqn-67"><mml:math id="mml-ieqn-67"><mml:mi>b</mml:mi></mml:math></inline-formula> to <inline-formula id="ieqn-68"><mml:math id="mml-ieqn-68"><mml:mi>a</mml:mi></mml:math></inline-formula>. The Eckert number, denoted by <inline-formula id="ieqn-69"><mml:math id="mml-ieqn-69"><mml:mi>E</mml:mi><mml:mi>c</mml:mi></mml:math></inline-formula>, is defined as <inline-formula id="ieqn-70"><mml:math id="mml-ieqn-70"><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msubsup><mml:mi>u</mml:mi><mml:mrow><mml:mi>w</mml:mi></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msubsup><mml:mrow><mml:msub><mml:mi>c</mml:mi><mml:mrow><mml:mi>p</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:mi>T</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow><mml:mo>)</mml:mo></mml:mrow></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula>, where <inline-formula id="ieqn-71"><mml:math id="mml-ieqn-71"><mml:mi>u</mml:mi></mml:math></inline-formula> is the velocity, <inline-formula id="ieqn-72"><mml:math id="mml-ieqn-72"><mml:mi>w</mml:mi></mml:math></inline-formula> is the enthalpy, specific heat is represented by <inline-formula id="ieqn-73"><mml:math id="mml-ieqn-73"><mml:msub><mml:mi>c</mml:mi><mml:mi>p</mml:mi></mml:msub></mml:math></inline-formula> the temperature of fluid is assigned as <inline-formula id="ieqn-74"><mml:math id="mml-ieqn-74"><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:math></inline-formula> and the free stream temperature is <inline-formula id="ieqn-75"><mml:math id="mml-ieqn-75"><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow></mml:msub></mml:math></inline-formula>. The Brownian motion parameter, <inline-formula id="ieqn-76"><mml:math id="mml-ieqn-76"><mml:mi>N</mml:mi><mml:mi>b</mml:mi><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mi>&#x03C4;</mml:mi><mml:msub><mml:mi>D</mml:mi><mml:mrow><mml:mi>B</mml:mi></mml:mrow></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>C</mml:mi><mml:mrow><mml:mi>w</mml:mi></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>C</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:mrow><mml:msub><mml:mi>&#x03BD;</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle></mml:math></inline-formula>, and the thermophoresis parameter, <inline-formula id="ieqn-77"><mml:math id="mml-ieqn-77"><mml:mi>N</mml:mi><mml:mi>t</mml:mi><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mi>&#x03C4;</mml:mi><mml:msub><mml:mi>D</mml:mi><mml:mrow><mml:mi>T</mml:mi></mml:mrow></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:mrow><mml:mrow><mml:msub><mml:mi>&#x03BD;</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow></mml:msub></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula>. The local heat source/sink parameter is given by <inline-formula id="ieqn-78"><mml:math id="mml-ieqn-78"><mml:mi>&#x03B3;</mml:mi><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:msub><mml:mi>Q</mml:mi><mml:mrow><mml:mn>0</mml:mn></mml:mrow></mml:msub><mml:msubsup><mml:mi>B</mml:mi><mml:mrow><mml:mn>0</mml:mn></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msubsup></mml:mrow><mml:mrow><mml:mi>a</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mi>&#x03C1;</mml:mi><mml:msub><mml:mi>c</mml:mi><mml:mrow><mml:mi>p</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mo stretchy="false">)</mml:mo><mml:mi>f</mml:mi></mml:msub></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula>. The Prandt number is denoted by <inline-formula id="ieqn-79"><mml:math id="mml-ieqn-79"><mml:mi>P</mml:mi><mml:mi>r</mml:mi><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:msub><mml:mi>&#x03BC;</mml:mi><mml:mrow><mml:mn>0</mml:mn></mml:mrow></mml:msub><mml:msub><mml:mi>c</mml:mi><mml:mrow><mml:mi>p</mml:mi></mml:mrow></mml:msub></mml:mrow><mml:msub><mml:mi>K</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle></mml:math></inline-formula>, while <inline-formula id="ieqn-80"><mml:math id="mml-ieqn-80"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub></mml:math></inline-formula> is the thermal number and is defined as <inline-formula id="ieqn-81"><mml:math id="mml-ieqn-81"><mml:msqrt><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mi>&#x03BD;</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mi>a</mml:mi></mml:mfrac></mml:mstyle></mml:msqrt><mml:mrow><mml:mo>(</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mi>h</mml:mi><mml:mi>k</mml:mi></mml:mfrac></mml:mstyle><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula>.</p>
</sec>
<sec id="s2_2">
<label>2.2</label>
<title>Mass Transfer Equation</title>
<p>The mass transfer equation in fluid mechanics describes the transport of a chemical species, such as mass or concentration, in a fluid. It is a fundamental equation that governs a variety of processes, including heat transfer, chemical reactions, and diffusion. After boundary layer approximation, the mass transfer equation [<xref ref-type="bibr" rid="ref-11">11</xref>] takes the following form:</p>
<p><disp-formula id="eqn-14"><label>(14)</label><mml:math id="mml-eqn-14" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:mi>u</mml:mi><mml:msub><mml:mi>C</mml:mi><mml:mi>x</mml:mi></mml:msub><mml:mo>+</mml:mo><mml:mi>v</mml:mi><mml:msub><mml:mi>C</mml:mi><mml:mi>y</mml:mi></mml:msub><mml:mo>=</mml:mo><mml:msub><mml:mi>D</mml:mi><mml:mi>B</mml:mi></mml:msub><mml:msub><mml:mi>C</mml:mi><mml:mrow><mml:mi>y</mml:mi><mml:mi>y</mml:mi></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:mrow><mml:mo>(</mml:mo><mml:mfrac><mml:msub><mml:mi>D</mml:mi><mml:mi>T</mml:mi></mml:msub><mml:msub><mml:mi>T</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub></mml:mfrac><mml:mo>)</mml:mo></mml:mrow><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi>y</mml:mi><mml:mi>y</mml:mi></mml:mrow></mml:msub></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>and the corresponding boundary conditions are</p>
<p><disp-formula id="eqn-15"><label>(15)</label><mml:math id="mml-eqn-15" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd /><mml:mtd><mml:mi></mml:mi><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>D</mml:mi><mml:mrow><mml:mi>B</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>C</mml:mi><mml:mi>y</mml:mi></mml:msub><mml:mo>=</mml:mo><mml:mo stretchy="false">[</mml:mo><mml:mi>C</mml:mi><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>C</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mo stretchy="false">]</mml:mo><mml:msub><mml:mi>h</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>w</mml:mi><mml:mi>h</mml:mi><mml:mi>e</mml:mi><mml:mi>n</mml:mi><mml:mspace width="1em" /><mml:mi>y</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mi>C</mml:mi><mml:mo>=</mml:mo><mml:msub><mml:mi>C</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mi>x</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>w</mml:mi><mml:mi>h</mml:mi><mml:mi>e</mml:mi><mml:mi>n</mml:mi><mml:mspace width="1em" /><mml:mi>y</mml:mi><mml:mo stretchy="false">&#x2192;</mml:mo><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>where <italic>C</italic> the concentration, <inline-formula id="ieqn-82"><mml:math id="mml-ieqn-82"><mml:msub><mml:mi>D</mml:mi><mml:mi>B</mml:mi></mml:msub></mml:math></inline-formula> is the diffusion coefficient, <italic>T</italic> is the temperature, the thermal diffusivity <inline-formula id="ieqn-83"><mml:math id="mml-ieqn-83"><mml:msub><mml:mi>D</mml:mi><mml:mi>T</mml:mi></mml:msub></mml:math></inline-formula>, the Brownian diffusion <inline-formula id="ieqn-84"><mml:math id="mml-ieqn-84"><mml:msub><mml:mi>D</mml:mi><mml:mi>B</mml:mi></mml:msub></mml:math></inline-formula>, and <inline-formula id="ieqn-85"><mml:math id="mml-ieqn-85"><mml:msub><mml:mi>T</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub></mml:math></inline-formula> is the free-stream temperature.</p>
<p>The following similarity transformation [<xref ref-type="bibr" rid="ref-11">11</xref>] in <xref ref-type="disp-formula" rid="eqn-14">Eq. (14)</xref>:</p>
<p><disp-formula id="eqn-16"><label>(16)</label><mml:math id="mml-eqn-16" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd /><mml:mtd><mml:mi>&#x03B7;</mml:mi><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msqrt><mml:mfrac><mml:mi>a</mml:mi><mml:msub><mml:mi>&#x03BD;</mml:mi><mml:mi>f</mml:mi></mml:msub></mml:mfrac></mml:msqrt><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>&#x03D5;</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mi>&#x03B7;</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mfrac><mml:mrow><mml:mi>C</mml:mi><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>C</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub></mml:mrow><mml:mrow><mml:msub><mml:mi>C</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>C</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub></mml:mrow></mml:mfrac><mml:mo>,</mml:mo></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mi>u</mml:mi><mml:mo>=</mml:mo><mml:mi>a</mml:mi><mml:mi>x</mml:mi><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>v</mml:mi><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msqrt><mml:mi>a</mml:mi><mml:msub><mml:mi>&#x03BD;</mml:mi><mml:mi>f</mml:mi></mml:msub></mml:msqrt><mml:mi>f</mml:mi><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>We get the following ODE with boundary conditions as</p>
<p><disp-formula id="eqn-17"><label>(17)</label><mml:math id="mml-eqn-17" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:msup><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mo>&#x2033;</mml:mo></mml:mrow></mml:msup><mml:mo>+</mml:mo><mml:mrow><mml:mo>(</mml:mo><mml:mfrac><mml:msub><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:msub><mml:msub><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:msub></mml:mfrac><mml:mo>)</mml:mo></mml:mrow><mml:msup><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mo>&#x2033;</mml:mo></mml:mrow></mml:msup><mml:mo>+</mml:mo><mml:mrow><mml:mtext>Pr&#xA0;</mml:mtext></mml:mrow><mml:mrow><mml:mtext>Le</mml:mtext></mml:mrow><mml:mi>f</mml:mi><mml:msup><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p><disp-formula id="eqn-18"><label>(18)</label><mml:math id="mml-eqn-18" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:msup><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mrow><mml:mo>(</mml:mo><mml:mn>0</mml:mn><mml:mo>)</mml:mo></mml:mrow><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>2</mml:mn></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mn>1</mml:mn><mml:mo>&#x2212;</mml:mo><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mn>0</mml:mn><mml:mo>)</mml:mo></mml:mrow><mml:mo>)</mml:mo></mml:mrow><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>&#x03D5;</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mi mathvariant="normal">&#x221E;</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mn>0.</mml:mn></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>where <inline-formula id="ieqn-86"><mml:math id="mml-ieqn-86"><mml:msub><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:msub></mml:math></inline-formula> and <inline-formula id="ieqn-87"><mml:math id="mml-ieqn-87"><mml:msub><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:msub></mml:math></inline-formula> are the Brownian motion and thermophoresis parameters, respectively, the Prandtl number <inline-formula id="ieqn-88"><mml:math id="mml-ieqn-88"><mml:mtext>Pr</mml:mtext></mml:math></inline-formula>, the concentration Biot number <inline-formula id="ieqn-89"><mml:math id="mml-ieqn-89"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>2</mml:mn></mml:msub></mml:math></inline-formula>, and the Lewis number <inline-formula id="ieqn-90"><mml:math id="mml-ieqn-90"><mml:mtext>Le</mml:mtext></mml:math></inline-formula> based on the thermal diffusion coefficient.</p>
</sec>
<sec id="s2_3">
<label>2.3</label>
<title>Gyrotactic Microorganisms</title>
<p>The gyrotactic microorganisms equation in fluids describes the movement and behavior of microorganisms in response to fluid flows and gravitational forces. This equation is important in understanding the dynamics of aquatic ecosystems and the biogeochemical cycling of nutrients. The gyrotactic microorganism concentration equation [<xref ref-type="bibr" rid="ref-23">23</xref>] is expressed below:</p>
<p><disp-formula id="eqn-19"><label>(19)</label><mml:math id="mml-eqn-19" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:mi>u</mml:mi><mml:msub><mml:mi>N</mml:mi><mml:mi>x</mml:mi></mml:msub><mml:mo>+</mml:mo><mml:mi>v</mml:mi><mml:msub><mml:mi>N</mml:mi><mml:mi>y</mml:mi></mml:msub><mml:mo>+</mml:mo><mml:mfrac><mml:mrow><mml:mi>b</mml:mi><mml:msub><mml:mi>W</mml:mi><mml:mi>c</mml:mi></mml:msub></mml:mrow><mml:mrow><mml:mo stretchy="false">(</mml:mo><mml:msub><mml:mi>C</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>C</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub><mml:mo stretchy="false">)</mml:mo></mml:mrow></mml:mfrac><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>N</mml:mi><mml:msub><mml:mi>C</mml:mi><mml:mi>y</mml:mi></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mi>y</mml:mi></mml:msub><mml:mo>=</mml:mo><mml:msub><mml:mi>D</mml:mi><mml:mi>m</mml:mi></mml:msub><mml:msub><mml:mi>N</mml:mi><mml:mrow><mml:mi>y</mml:mi><mml:mi>y</mml:mi></mml:mrow></mml:msub><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>and the corresponding boundary conditions are</p>
<p><disp-formula id="eqn-20"><label>(20)</label><mml:math id="mml-eqn-20" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd /><mml:mtd><mml:mi></mml:mi><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>D</mml:mi><mml:mrow><mml:mi>m</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>N</mml:mi><mml:mi>y</mml:mi></mml:msub><mml:mo>=</mml:mo><mml:mo stretchy="false">[</mml:mo><mml:mi>N</mml:mi><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>N</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mo stretchy="false">]</mml:mo><mml:msub><mml:mi>h</mml:mi><mml:mrow><mml:mn>3</mml:mn></mml:mrow></mml:msub><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>w</mml:mi><mml:mi>h</mml:mi><mml:mi>e</mml:mi><mml:mi>n</mml:mi><mml:mspace width="1em" /><mml:mi>y</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mi>N</mml:mi><mml:mo>=</mml:mo><mml:msub><mml:mi>N</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>w</mml:mi><mml:mi>h</mml:mi><mml:mi>e</mml:mi><mml:mi>n</mml:mi><mml:mspace width="1em" /><mml:mi>y</mml:mi><mml:mo stretchy="false">&#x2192;</mml:mo><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>where <inline-formula id="ieqn-91"><mml:math id="mml-ieqn-91"><mml:msub><mml:mi>D</mml:mi><mml:mi>m</mml:mi></mml:msub></mml:math></inline-formula> is the diffusivity of microorganism, <inline-formula id="ieqn-92"><mml:math id="mml-ieqn-92"><mml:msub><mml:mi>h</mml:mi><mml:mn>3</mml:mn></mml:msub></mml:math></inline-formula> is the microorganisms transfer coefficients and <inline-formula id="ieqn-93"><mml:math id="mml-ieqn-93"><mml:msub><mml:mi>N</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub></mml:math></inline-formula> is the ambient microorganism concentration. Using the following similarity transformation [<xref ref-type="bibr" rid="ref-23">23</xref>] in <xref ref-type="disp-formula" rid="eqn-19">Eq. (19)</xref>:</p>
<p><disp-formula id="eqn-21"><label>(21)</label><mml:math id="mml-eqn-21" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd /><mml:mtd><mml:mi>&#x03B7;</mml:mi><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msqrt><mml:mfrac><mml:mi>a</mml:mi><mml:msub><mml:mi>&#x03BD;</mml:mi><mml:mi>f</mml:mi></mml:msub></mml:mfrac></mml:msqrt><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>&#x03C7;</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mi>&#x03B7;</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mfrac><mml:mrow><mml:mi>N</mml:mi><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>N</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub></mml:mrow><mml:mrow><mml:msub><mml:mi>N</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>N</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub></mml:mrow></mml:mfrac><mml:mo>,</mml:mo></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mi>u</mml:mi><mml:mo>=</mml:mo><mml:mi>a</mml:mi><mml:mi>x</mml:mi><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mi>&#x03B7;</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>v</mml:mi><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msqrt><mml:mi>a</mml:mi><mml:msub><mml:mi>&#x03BD;</mml:mi><mml:mi>f</mml:mi></mml:msub></mml:msqrt><mml:mi>f</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mi>&#x03B7;</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>we get</p>
<p><disp-formula id="eqn-22"><label>(22)</label><mml:math id="mml-eqn-22" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:msup><mml:mi>&#x03C7;</mml:mi><mml:mrow><mml:mo>&#x2033;</mml:mo></mml:mrow></mml:msup><mml:mo>+</mml:mo><mml:mi>L</mml:mi><mml:mi>b</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mi>f</mml:mi><mml:msup><mml:mi>&#x03C7;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">)</mml:mo><mml:mo>&#x2212;</mml:mo><mml:mi>P</mml:mi><mml:mi>e</mml:mi><mml:mo stretchy="false">[</mml:mo><mml:msup><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mo>&#x2033;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mi>&#x03C7;</mml:mi><mml:mo>+</mml:mo><mml:mi mathvariant="normal">&#x03A9;</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mo>+</mml:mo><mml:msup><mml:mi>&#x03C7;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:msup><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">]</mml:mo><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p><disp-formula id="eqn-23"><label>(23)</label><mml:math id="mml-eqn-23" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:msup><mml:mi>&#x03C7;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mrow><mml:mo>(</mml:mo><mml:mn>0</mml:mn><mml:mo>)</mml:mo></mml:mrow><mml:mo>=</mml:mo><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>3</mml:mn></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mn>1</mml:mn><mml:mo>&#x2212;</mml:mo><mml:mi>&#x03C7;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mn>0</mml:mn><mml:mo>)</mml:mo></mml:mrow><mml:mo>)</mml:mo></mml:mrow><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>&#x03C7;</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mi mathvariant="normal">&#x221E;</mml:mi><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mn>0.</mml:mn></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>where <inline-formula id="ieqn-94"><mml:math id="mml-ieqn-94"><mml:mi>L</mml:mi><mml:mi>b</mml:mi><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mi>k</mml:mi><mml:mrow><mml:mi>&#x03C1;</mml:mi><mml:msub><mml:mi>c</mml:mi><mml:mi>p</mml:mi></mml:msub><mml:msub><mml:mi>D</mml:mi><mml:mi>m</mml:mi></mml:msub></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula> represents the bioconvection Lewis number, <inline-formula id="ieqn-95"><mml:math id="mml-ieqn-95"><mml:mi>P</mml:mi><mml:mi>e</mml:mi><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mi>b</mml:mi><mml:msub><mml:mi>W</mml:mi><mml:mi>c</mml:mi></mml:msub></mml:mrow><mml:msub><mml:mi>D</mml:mi><mml:mi>m</mml:mi></mml:msub></mml:mfrac></mml:mstyle></mml:math></inline-formula> the bioconvection Peclet number, and <inline-formula id="ieqn-96"><mml:math id="mml-ieqn-96"><mml:mi mathvariant="normal">&#x03A9;</mml:mi><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mi>N</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub><mml:mrow><mml:msub><mml:mi>N</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>N</mml:mi><mml:mn>0</mml:mn></mml:msub></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula> the concentration difference parameter.</p>
</sec>
<sec id="s2_4">
<label>2.4</label>
<title>Physical Quantities</title>
<p>Skin friction coefficient, Nusselt number, Sherwood number and Density number are defined below:</p>
<p><disp-formula id="eqn-24"><label>(24)</label><mml:math id="mml-eqn-24" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd /><mml:mtd><mml:msub><mml:mi>C</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mo>=</mml:mo><mml:mfrac><mml:msub><mml:mi>&#x03C4;</mml:mi><mml:mi>w</mml:mi></mml:msub><mml:mrow><mml:mi>&#x03C1;</mml:mi><mml:msubsup><mml:mi>u</mml:mi><mml:mi>w</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msubsup></mml:mrow></mml:mfrac><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>N</mml:mi><mml:msub><mml:mi>u</mml:mi><mml:mi>x</mml:mi></mml:msub><mml:mo>=</mml:mo><mml:mfrac><mml:mrow><mml:mi>x</mml:mi><mml:msub><mml:mi>q</mml:mi><mml:mi>w</mml:mi></mml:msub></mml:mrow><mml:mrow><mml:mi>K</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>T</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>T</mml:mi><mml:mn>0</mml:mn></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:mrow></mml:mfrac><mml:mo>,</mml:mo></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mi>S</mml:mi><mml:msub><mml:mi>h</mml:mi><mml:mi>x</mml:mi></mml:msub><mml:mo>=</mml:mo><mml:mfrac><mml:mrow><mml:mi>x</mml:mi><mml:msub><mml:mi>j</mml:mi><mml:mi>w</mml:mi></mml:msub></mml:mrow><mml:mrow><mml:msub><mml:mi>D</mml:mi><mml:mrow><mml:mi>B</mml:mi></mml:mrow></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>C</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>C</mml:mi><mml:mn>0</mml:mn></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:mrow></mml:mfrac><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>D</mml:mi><mml:msub><mml:mi>n</mml:mi><mml:mi>x</mml:mi></mml:msub><mml:mo>=</mml:mo><mml:mfrac><mml:mrow><mml:mi>x</mml:mi><mml:msub><mml:mi>q</mml:mi><mml:mi>n</mml:mi></mml:msub></mml:mrow><mml:mrow><mml:msub><mml:mi>D</mml:mi><mml:mi>m</mml:mi></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>N</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>N</mml:mi><mml:mn>0</mml:mn></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:mrow></mml:mfrac><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>where</p>
<p><disp-formula id="eqn-25"><label>(25)</label><mml:math id="mml-eqn-25" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd /><mml:mtd><mml:msub><mml:mi>&#x03C4;</mml:mi><mml:mi>w</mml:mi></mml:msub><mml:mo>=</mml:mo><mml:msub><mml:mrow><mml:mo>[</mml:mo><mml:msub><mml:mi>&#x03BC;</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:msub><mml:mi>u</mml:mi><mml:mi>y</mml:mi></mml:msub><mml:mo>+</mml:mo><mml:msub><mml:mi>k</mml:mi><mml:mn>0</mml:mn></mml:msub><mml:msub><mml:mi>&#x03C1;</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>u</mml:mi><mml:msub><mml:mi>u</mml:mi><mml:mrow><mml:mi>x</mml:mi><mml:mi>y</mml:mi></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:mi>v</mml:mi><mml:msub><mml:mi>u</mml:mi><mml:mrow><mml:mi>y</mml:mi><mml:mi>y</mml:mi></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:mn>2</mml:mn><mml:msub><mml:mi>u</mml:mi><mml:mi>x</mml:mi></mml:msub><mml:msub><mml:mi>u</mml:mi><mml:mi>y</mml:mi></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mo>]</mml:mo></mml:mrow><mml:mrow><mml:mi>y</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:mrow></mml:msub><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:msub><mml:mi>q</mml:mi><mml:mi>w</mml:mi></mml:msub><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:mi>k</mml:mi><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>T</mml:mi><mml:mi>y</mml:mi></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mi>y</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:mrow></mml:msub><mml:mo>,</mml:mo></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:msub><mml:mi>j</mml:mi><mml:mi>w</mml:mi></mml:msub><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>D</mml:mi><mml:mrow><mml:mi>B</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>C</mml:mi><mml:mi>y</mml:mi></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mi>y</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:mrow></mml:msub><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:msub><mml:mi>q</mml:mi><mml:mi>n</mml:mi></mml:msub><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>D</mml:mi><mml:mi>m</mml:mi></mml:msub><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>N</mml:mi><mml:mi>y</mml:mi></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mi>y</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:mrow></mml:msub><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>Now, the dimensionless forms are defined below:</p>
<p><disp-formula id="eqn-26"><label>(26)</label><mml:math id="mml-eqn-26" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd /><mml:mtd><mml:mi>C</mml:mi><mml:msub><mml:mi>f</mml:mi><mml:mrow><mml:mi>x</mml:mi></mml:mrow></mml:msub><mml:msqrt><mml:mi>R</mml:mi><mml:msub><mml:mi>e</mml:mi><mml:mi>x</mml:mi></mml:msub></mml:msqrt><mml:mo>=</mml:mo><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2033;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>+</mml:mo><mml:mi>K</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mn>3</mml:mn><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2033;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>&#x2212;</mml:mo><mml:mi>f</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2034;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>)</mml:mo></mml:mrow><mml:mo>,</mml:mo></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mi>N</mml:mi><mml:msub><mml:mi>u</mml:mi><mml:mi>x</mml:mi></mml:msub><mml:mi>R</mml:mi><mml:msubsup><mml:mi>e</mml:mi><mml:mi>x</mml:mi><mml:mrow><mml:mfrac><mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mn>1</mml:mn></mml:mrow><mml:mn>2</mml:mn></mml:mfrac></mml:mrow></mml:msubsup><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msup><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>S</mml:mi><mml:msub><mml:mi>h</mml:mi><mml:mi>x</mml:mi></mml:msub><mml:mi>R</mml:mi><mml:msubsup><mml:mi>e</mml:mi><mml:mi>x</mml:mi><mml:mrow><mml:mfrac><mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mn>1</mml:mn></mml:mrow><mml:mn>2</mml:mn></mml:mfrac></mml:mrow></mml:msubsup><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msup><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>D</mml:mi><mml:msub><mml:mi>n</mml:mi><mml:mi>x</mml:mi></mml:msub><mml:mi>R</mml:mi><mml:msubsup><mml:mi>e</mml:mi><mml:mi>x</mml:mi><mml:mrow><mml:mfrac><mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mn>1</mml:mn></mml:mrow><mml:mn>2</mml:mn></mml:mfrac></mml:mrow></mml:msubsup><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msup><mml:mi>&#x03C7;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>.</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>where <inline-formula id="ieqn-97"><mml:math id="mml-ieqn-97"><mml:mi>R</mml:mi><mml:msub><mml:mi>e</mml:mi><mml:mi>x</mml:mi></mml:msub><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:msub><mml:mi>u</mml:mi><mml:mi>w</mml:mi></mml:msub><mml:mi>x</mml:mi></mml:mrow><mml:mi>&#x03BD;</mml:mi></mml:mfrac></mml:mstyle></mml:math></inline-formula> represents the Reynolds number.</p>
</sec>
</sec>
<sec id="s3">
<label>3</label>
<title>Solution Methodology</title>
<p>The governing equations given by <xref ref-type="disp-formula" rid="eqn-6">Eqs. (6)</xref>, <xref ref-type="disp-formula" rid="eqn-12">(12)</xref>, <xref ref-type="disp-formula" rid="eqn-17">(17)</xref>, <xref ref-type="disp-formula" rid="eqn-22">(22)</xref> with boundary conditions specified in <xref ref-type="disp-formula" rid="eqn-7">Eqs. (7)</xref>, <xref ref-type="disp-formula" rid="eqn-13">(13)</xref>, <xref ref-type="disp-formula" rid="eqn-18">(18)</xref>, <xref ref-type="disp-formula" rid="eqn-23">(23)</xref>, respectively, were solved numerically using the built-in MATLAB function <italic>bvp4c</italic>. The bvp4c finite difference solver relies on the three-stage Lobatto IIIa collocation formula, ensuring a C1-continuous solution that uniformly maintains fourth-order accuracy throughout the integration interval. To manage errors and select an appropriate mesh, the solver employs the residual of the continuous solution. The integration interval is subdivided into smaller subintervals using a mesh of data points. The solver then tackles a comprehensive system of algebraic equations formed by combining boundary conditions and collocation requirements across these subintervals. Error assessment is carried out for each subinterval, and if the computed solution does not meet the predefined tolerance criteria, the solver iteratively adjusts the mesh. To initiate this iterative process, initial approximations of the solution at the mesh points are required. Achieving asymptotic behavior entails configuring the solution tolerance rate to be as stringent as <inline-formula id="ieqn-98"><mml:math id="mml-ieqn-98"><mml:msup><mml:mn>10</mml:mn><mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mn>6</mml:mn></mml:mrow></mml:msup></mml:math></inline-formula>. Consequently, the solver continues its iterations until the solution reaches a level of accuracy where the relative error falls within <inline-formula id="ieqn-99"><mml:math id="mml-ieqn-99"><mml:msup><mml:mn>10</mml:mn><mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mn>6</mml:mn></mml:mrow></mml:msup></mml:math></inline-formula>. The aforementioned equations converted into a first-order system of ODEs before applying this method as</p>
<p><disp-formula id="eqn-27"><label>(27)</label><mml:math id="mml-eqn-27" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:msub><mml:mi>y</mml:mi><mml:mn>1</mml:mn></mml:msub><mml:mo>=</mml:mo><mml:mi>f</mml:mi><mml:mo>,</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo>,</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>3</mml:mn></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2033;</mml:mo></mml:mrow></mml:msup><mml:mo>,</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>4</mml:mn></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:mi>&#x03B8;</mml:mi><mml:mo>,</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>5</mml:mn></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:msup><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo>,</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>6</mml:mn></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:mi>&#x03D5;</mml:mi><mml:mo>,</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>7</mml:mn></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:msup><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo>,</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>8</mml:mn></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:mi>&#x03C7;</mml:mi><mml:mo>,</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>9</mml:mn></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:msup><mml:mi>&#x03C7;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>To get the numerical answer, a new set of variables is defined in MATLAB as the following:</p>
<p><disp-formula id="eqn-28"><label>(28)</label><mml:math id="mml-eqn-28" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd /><mml:mtd><mml:msubsup><mml:mi>y</mml:mi><mml:mn>1</mml:mn><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msubsup><mml:mo>=</mml:mo><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:msubsup><mml:mi>y</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msubsup><mml:mo>=</mml:mo><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2033;</mml:mo></mml:mrow></mml:msup><mml:mo>,</mml:mo></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:msubsup><mml:mi>y</mml:mi><mml:mrow><mml:mn>3</mml:mn></mml:mrow><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msubsup><mml:mo>=</mml:mo><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2034;</mml:mo></mml:mrow></mml:msup><mml:mo>=</mml:mo><mml:msup><mml:mi>e</mml:mi><mml:mrow><mml:mi>&#x03B1;</mml:mi><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>4</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:msup><mml:mrow><mml:mo>[</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>1</mml:mn></mml:mrow></mml:msub><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>3</mml:mn></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:msubsup><mml:mi>y</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msubsup><mml:mo>&#x2212;</mml:mo><mml:mi>K</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mn>2</mml:mn><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>3</mml:mn></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>1</mml:mn></mml:mrow></mml:msub><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>3</mml:mn></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msubsup><mml:mi>y</mml:mi><mml:mrow><mml:mn>3</mml:mn></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msubsup><mml:mo>)</mml:mo></mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mrow><mml:mo>(</mml:mo><mml:mi>M</mml:mi><mml:mo>+</mml:mo><mml:msup><mml:mi>e</mml:mi><mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mi>&#x03B1;</mml:mi><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>4</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:msup><mml:mi>&#x03B4;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03BB;</mml:mi><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mo fence="true" stretchy="true" symmetric="true"></mml:mo></mml:mrow></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mspace width="2em" /><mml:mspace width="2em" /><mml:mtext>&#x00A0;</mml:mtext><mml:mrow><mml:mo fence="true" stretchy="true" symmetric="true"></mml:mo><mml:mo>&#x2212;</mml:mo><mml:msup><mml:mi>&#x03BB;</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mo>+</mml:mo><mml:msup><mml:mi>e</mml:mi><mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mi>&#x03B1;</mml:mi><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>4</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:msup><mml:mi>&#x03B1;</mml:mi><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>5</mml:mn></mml:mrow></mml:msub><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>3</mml:mn></mml:mrow></mml:msub><mml:mo>]</mml:mo></mml:mrow><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p><disp-formula id="eqn-29"><label>(29)</label><mml:math id="mml-eqn-29" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:msubsup><mml:mi>y</mml:mi><mml:mn>4</mml:mn><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msubsup><mml:mo>=</mml:mo><mml:msup><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo>,</mml:mo><mml:msubsup><mml:mi>y</mml:mi><mml:mn>5</mml:mn><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msubsup><mml:mo>=</mml:mo><mml:msup><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>&#x2033;</mml:mo></mml:mrow></mml:msup></mml:mtd><mml:mtd><mml:mi></mml:mi><mml:mo>=</mml:mo><mml:mfrac><mml:mn>1</mml:mn><mml:mrow><mml:mn>1</mml:mn><mml:mo>+</mml:mo><mml:mi>&#x03B5;</mml:mi><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>4</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:mfrac><mml:mrow><mml:mo>[</mml:mo><mml:mo>&#x2212;</mml:mo><mml:mi>&#x03B5;</mml:mi><mml:msubsup><mml:mi>y</mml:mi><mml:mrow><mml:mn>5</mml:mn></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msubsup><mml:mo>&#x2212;</mml:mo><mml:mi>P</mml:mi><mml:mi>r</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>1</mml:mn></mml:mrow></mml:msub><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>5</mml:mn></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:mi>E</mml:mi><mml:mi>c</mml:mi><mml:msubsup><mml:mi>y</mml:mi><mml:mrow><mml:mn>3</mml:mn></mml:mrow><mml:mn>2</mml:mn></mml:msubsup><mml:mo>+</mml:mo><mml:mi>M</mml:mi><mml:mi>E</mml:mi><mml:mi>c</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mi>&#x03BB;</mml:mi><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:msup><mml:mo stretchy="false">)</mml:mo><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mo>+</mml:mo><mml:mi>N</mml:mi><mml:mi>b</mml:mi><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>5</mml:mn></mml:mrow></mml:msub><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>7</mml:mn></mml:mrow></mml:msub><mml:mo fence="true" stretchy="true" symmetric="true"></mml:mo></mml:mrow><mml:mo fence="true" stretchy="true" symmetric="true"></mml:mo></mml:mrow></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mspace width="1em" /><mml:mrow><mml:mo fence="true" stretchy="true" symmetric="true"></mml:mo><mml:mrow><mml:mo fence="true" stretchy="true" symmetric="true"></mml:mo><mml:mo>+</mml:mo><mml:mi>N</mml:mi><mml:mi>t</mml:mi><mml:msubsup><mml:mi>y</mml:mi><mml:mrow><mml:mn>5</mml:mn></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msubsup><mml:mo>+</mml:mo><mml:mi>&#x03B3;</mml:mi><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>4</mml:mn></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mo>]</mml:mo></mml:mrow><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p><disp-formula id="eqn-30"><label>(30)</label><mml:math id="mml-eqn-30" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:msubsup><mml:mi>y</mml:mi><mml:mn>6</mml:mn><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msubsup><mml:mo>=</mml:mo><mml:msup><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:msubsup><mml:mi>y</mml:mi><mml:mn>7</mml:mn><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msubsup><mml:mo>=</mml:mo><mml:msup><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mo>&#x2033;</mml:mo></mml:mrow></mml:msup><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:mi>L</mml:mi><mml:mi>e</mml:mi><mml:mi>P</mml:mi><mml:mi>r</mml:mi><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>1</mml:mn></mml:mrow></mml:msub><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>7</mml:mn></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:mfrac><mml:msub><mml:mi>N</mml:mi><mml:mrow><mml:mi>t</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>N</mml:mi><mml:mrow><mml:mi>b</mml:mi></mml:mrow></mml:msub></mml:mfrac><mml:msubsup><mml:mi>y</mml:mi><mml:mrow><mml:mn>5</mml:mn></mml:mrow><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msubsup><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p><disp-formula id="eqn-31"><label>(31)</label><mml:math id="mml-eqn-31" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd><mml:msubsup><mml:mi>y</mml:mi><mml:mrow><mml:mn>8</mml:mn></mml:mrow><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msubsup><mml:mo>=</mml:mo><mml:msup><mml:mi>&#x03C7;</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:msubsup><mml:mi>y</mml:mi><mml:mrow><mml:mn>9</mml:mn></mml:mrow><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msubsup><mml:mo>=</mml:mo><mml:msup><mml:mi>&#x03C7;</mml:mi><mml:mrow><mml:mo>&#x2033;</mml:mo></mml:mrow></mml:msup><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:mi>L</mml:mi><mml:mi>b</mml:mi><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>1</mml:mn></mml:mrow></mml:msub><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>9</mml:mn></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:mi>P</mml:mi><mml:mi>e</mml:mi><mml:mrow><mml:mo>[</mml:mo><mml:msubsup><mml:mi>y</mml:mi><mml:mrow><mml:mn>7</mml:mn></mml:mrow><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msubsup><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>8</mml:mn></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:mi mathvariant="normal">&#x03A9;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mo>+</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>9</mml:mn></mml:mrow></mml:msub><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>7</mml:mn></mml:mrow></mml:msub><mml:mo>]</mml:mo></mml:mrow><mml:mo>,</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>The boundary conditions are written in boundary value residual form, as required by <inline-formula id="ieqn-100"><mml:math id="mml-ieqn-100"><mml:mi>b</mml:mi><mml:mi>v</mml:mi><mml:mi>p</mml:mi><mml:mn>4</mml:mn><mml:mi>c</mml:mi></mml:math></inline-formula>, as shown below:</p>
<p><disp-formula id="eqn-32"><label>(32)</label><mml:math id="mml-eqn-32" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd /><mml:mtd><mml:mi>y</mml:mi><mml:mn>0</mml:mn><mml:mo stretchy="false">(</mml:mo><mml:mn>1</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>y</mml:mi><mml:mn>0</mml:mn><mml:mo stretchy="false">(</mml:mo><mml:mn>2</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>&#x2212;</mml:mo><mml:mn>1</mml:mn><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>y</mml:mi><mml:mn>0</mml:mn><mml:mo stretchy="false">(</mml:mo><mml:mn>5</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>+</mml:mo><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mn>1</mml:mn><mml:mo>&#x2212;</mml:mo><mml:mi>y</mml:mi><mml:mn>0</mml:mn><mml:mo stretchy="false">(</mml:mo><mml:mn>4</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mi>y</mml:mi><mml:mn>0</mml:mn><mml:mo stretchy="false">(</mml:mo><mml:mn>7</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>+</mml:mo><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>2</mml:mn></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mn>1</mml:mn><mml:mo>&#x2212;</mml:mo><mml:mi>y</mml:mi><mml:mn>0</mml:mn><mml:mo stretchy="false">(</mml:mo><mml:mn>6</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>y</mml:mi><mml:mn>0</mml:mn><mml:mo stretchy="false">(</mml:mo><mml:mn>9</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>+</mml:mo><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>3</mml:mn></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mn>1</mml:mn><mml:mo>&#x2212;</mml:mo><mml:mi>y</mml:mi><mml:mn>0</mml:mn><mml:mo stretchy="false">(</mml:mo><mml:mn>8</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>y</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mn>2</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>&#x2212;</mml:mo><mml:mi>&#x03BB;</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mi>y</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mn>4</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>y</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mn>6</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>y</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mn>8</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>=</mml:mo><mml:mn>0.</mml:mn></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>The physical quantities converted as below:</p>
<p><disp-formula id="eqn-33"><label>(33)</label><mml:math id="mml-eqn-33" display="block"><mml:mtable columnalign="right left right left right left right left right left right left" rowspacing="3pt" columnspacing="0em 2em 0em 2em 0em 2em 0em 2em 0em 2em 0em" displaystyle="true"><mml:mtr><mml:mtd /><mml:mtd><mml:mi>C</mml:mi><mml:msub><mml:mi>f</mml:mi><mml:mrow><mml:mi>x</mml:mi></mml:mrow></mml:msub><mml:msqrt><mml:mi>R</mml:mi><mml:msub><mml:mi>e</mml:mi><mml:mi>x</mml:mi></mml:msub></mml:msqrt><mml:mo>=</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>3</mml:mn></mml:mrow></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>+</mml:mo><mml:mi>K</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mn>3</mml:mn><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>3</mml:mn></mml:mrow></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msubsup><mml:mi>y</mml:mi><mml:mrow><mml:mn>3</mml:mn></mml:mrow><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msubsup><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>1</mml:mn></mml:mrow></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>)</mml:mo></mml:mrow><mml:mo>,</mml:mo></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mi>N</mml:mi><mml:msub><mml:mi>u</mml:mi><mml:mi>x</mml:mi></mml:msub><mml:mi>R</mml:mi><mml:msubsup><mml:mi>e</mml:mi><mml:mi>x</mml:mi><mml:mrow><mml:mfrac><mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mn>1</mml:mn></mml:mrow><mml:mn>2</mml:mn></mml:mfrac></mml:mrow></mml:msubsup><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>5</mml:mn></mml:mrow></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>S</mml:mi><mml:msub><mml:mi>h</mml:mi><mml:mi>x</mml:mi></mml:msub><mml:mi>R</mml:mi><mml:msubsup><mml:mi>e</mml:mi><mml:mi>x</mml:mi><mml:mrow><mml:mfrac><mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mn>1</mml:mn></mml:mrow><mml:mn>2</mml:mn></mml:mfrac></mml:mrow></mml:msubsup><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>7</mml:mn></mml:mrow></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>,</mml:mo><mml:mspace width="1em" /><mml:mi>D</mml:mi><mml:msub><mml:mi>n</mml:mi><mml:mi>x</mml:mi></mml:msub><mml:mi>R</mml:mi><mml:msubsup><mml:mi>e</mml:mi><mml:mi>x</mml:mi><mml:mrow><mml:mfrac><mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mn>1</mml:mn></mml:mrow><mml:mn>2</mml:mn></mml:mfrac></mml:mrow></mml:msubsup><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mn>9</mml:mn></mml:mrow></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mn>0</mml:mn><mml:mo stretchy="false">)</mml:mo><mml:mo>.</mml:mo></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
</sec>
<sec id="s4">
<label>4</label>
<title>Numerical Results and Discussion</title>
<p>The numerical results from our work and research questions are thoroughly discussed in this section, along with their physical importance and applicability to a wider range of fluid dynamics and heat transport problems. Our findings cover a wide range of flow and transport processes in a porous viscoelastic fluid-saturated medium affected by magnetic fields, heat effects, and microorganism dynamics.</p>
<p>For different values of the ratio parameter <inline-formula id="ieqn-101"><mml:math id="mml-ieqn-101"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula>, the value of the skin friction coefficient is calculated as mentioned in <xref ref-type="table" rid="table-1">Table 1</xref>. To validate our findings, results are compared with the previous research.</p>
<table-wrap id="table-1">
<label>Table 1</label>
<caption>
<title>Comparison of <inline-formula id="ieqn-102"><mml:math id="mml-ieqn-102"><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&quot;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mi>&#x03B7;</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula> with previously published data [<xref ref-type="bibr" rid="ref-11">11</xref>] by considering <inline-formula id="ieqn-103"><mml:math id="mml-ieqn-103"><mml:mi>&#x03B4;</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:math></inline-formula>, <inline-formula id="ieqn-104"><mml:math id="mml-ieqn-104"><mml:mi>&#x03B1;</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:math></inline-formula>, <inline-formula id="ieqn-105"><mml:math id="mml-ieqn-105"><mml:mi>M</mml:mi><mml:mo>=</mml:mo><mml:mn>0.1</mml:mn></mml:math></inline-formula>, <inline-formula id="ieqn-106"><mml:math id="mml-ieqn-106"><mml:mi>K</mml:mi><mml:mo>=</mml:mo><mml:mn>0.1</mml:mn></mml:math></inline-formula></title>
</caption>
<table frame="hsides">
<colgroup>
<col align="left"/>
<col align="left"/>
<col align="left"/>
</colgroup>
<thead>
<tr>
<th><inline-formula id="ieqn-107"><mml:math id="mml-ieqn-107"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula></th>
<th>Ali et al. [<xref ref-type="bibr" rid="ref-11">11</xref>]</th>
<th>Present work</th>
</tr>
</thead>
<tbody>
<tr>
<td>0.1</td>
<td>&#x2212;1.41633</td>
<td>&#x2212;1.4160</td>
</tr>
<tr>
<td>0.2</td>
<td>&#x2212;1.33319</td>
<td>&#x2212;1.3331</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>Multiple tables show the outcomes of our numerical calculations. <xref ref-type="table" rid="table-2">Tables 2</xref>&#x2013;<xref ref-type="table" rid="table-5">5</xref> present the skin friction coefficient, local Nusselt number, local Sherwood number, and local density number of motile microorganisms, in that order. Skin friction coefficient parameter is vital for describing the drag force applied by the fluid to a solid surface and is used in many different engineering applications. Skin friction is observed to increase with increases in the ratio parameter <inline-formula id="ieqn-108"><mml:math id="mml-ieqn-108"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula>, whereas declines are observed with increases in the viscosity parameter <inline-formula id="ieqn-109"><mml:math id="mml-ieqn-109"><mml:mi>&#x03B1;</mml:mi></mml:math></inline-formula>, the local Darcy number <inline-formula id="ieqn-110"><mml:math id="mml-ieqn-110"><mml:mi>&#x03B4;</mml:mi></mml:math></inline-formula>, and the magnetic number <italic>M</italic>. The viscoelastic parameter <italic>K</italic> influences the flow characteristics near the heated sheet by affecting the boundary layer behavior. An increase in <italic>K</italic> leads to a reduction in the thickness of the velocity boundary layer region. This results in a decrease in fluid velocity near the solid surface. Additionally, the presence of the magnetic field in the presence of a porous surface significantly increases fluid velocity. It is observed that, on the specific value of <italic>M</italic>, fluid velocity can increase by approximately 25% to 45%. This suggests that magnetic effects play a crucial role in enhancing fluid motion under these conditions.</p>
<table-wrap id="table-2">
<label>Table 2</label>
<caption>
<title>Analyzing the effects of several factors on the skin friction coefficient while taking into account <inline-formula id="ieqn-111"><mml:math id="mml-ieqn-111"><mml:mi>&#x03B5;</mml:mi><mml:mo>=</mml:mo><mml:mi>E</mml:mi><mml:mi>c</mml:mi><mml:mo>=</mml:mo><mml:mi>N</mml:mi><mml:mi>b</mml:mi><mml:mo>=</mml:mo><mml:mi>N</mml:mi><mml:mi>t</mml:mi><mml:mo>=</mml:mo><mml:mi mathvariant="normal">&#x03A9;</mml:mi><mml:mo>=</mml:mo><mml:mn>0.2</mml:mn></mml:math></inline-formula>, <inline-formula id="ieqn-112"><mml:math id="mml-ieqn-112"><mml:mi>&#x03B3;</mml:mi><mml:mo>=</mml:mo><mml:mi>L</mml:mi><mml:mi>e</mml:mi><mml:mo>=</mml:mo><mml:mi>P</mml:mi><mml:mi>e</mml:mi><mml:mo>=</mml:mo><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub><mml:mo>=</mml:mo><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>2</mml:mn></mml:msub><mml:mo>=</mml:mo><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>3</mml:mn></mml:msub><mml:mo>=</mml:mo><mml:mn>0.1</mml:mn></mml:math></inline-formula>, <inline-formula id="ieqn-113"><mml:math id="mml-ieqn-113"><mml:mi>L</mml:mi><mml:mi>b</mml:mi><mml:mo>=</mml:mo><mml:mn>1</mml:mn></mml:math></inline-formula>, <inline-formula id="ieqn-114"><mml:math id="mml-ieqn-114"><mml:mi>P</mml:mi><mml:mi>r</mml:mi><mml:mo>=</mml:mo><mml:mn>6</mml:mn></mml:math></inline-formula><break/></title>
</caption>
<table frame="hsides">
<colgroup>
<col align="left"/>
<col align="left"/>
<col align="left"/>
<col align="left"/>
<col align="left"/>
<col align="left"/>
</colgroup>
<thead>
<tr>
<th><inline-formula id="ieqn-115"><mml:math id="mml-ieqn-115"><mml:mi>&#x03B1;</mml:mi></mml:math></inline-formula></th>
<th><italic>K</italic></th>
<th><italic>M</italic></th>
<th><inline-formula id="ieqn-116"><mml:math id="mml-ieqn-116"><mml:mi>&#x03B4;</mml:mi></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-117"><mml:math id="mml-ieqn-117"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-118"><mml:math id="mml-ieqn-118"><mml:msub><mml:mi>C</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msqrt><mml:msub><mml:mi>R</mml:mi><mml:mrow><mml:mi>e</mml:mi></mml:mrow></mml:msub><mml:mi>x</mml:mi></mml:msqrt></mml:math></inline-formula></th>
</tr>
</thead>
<tbody>
<tr>
<td>0.0</td>
<td>0.1</td>
<td>0.1</td>
<td>0.2</td>
<td>0.1</td>
<td>&#x2212;1.5209</td>
</tr>
<tr>
<td>0.5</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>&#x2212;1.7420</td>
</tr>
<tr>
<td>1.0</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>&#x2212;2.1234</td>
</tr>
<tr>
<td>0.5</td>
<td>0.1</td>
<td>0.1</td>
<td>0.2</td>
<td>0.1</td>
<td>&#x2212;1.7420</td>
</tr>
<tr>
<td></td>
<td>0.5</td>
<td></td>
<td></td>
<td></td>
<td>&#x2212;3.1154</td>
</tr>
<tr>
<td></td>
<td>0.9</td>
<td></td>
<td></td>
<td></td>
<td>&#x2212;5.1556</td>
</tr>
<tr>
<td>0.5</td>
<td>0.1</td>
<td>0.1</td>
<td>0.2</td>
<td></td>
<td>&#x2212;1.7420</td>
</tr>
<tr>
<td></td>
<td></td>
<td>0.3</td>
<td></td>
<td></td>
<td>&#x2212;2.0553</td>
</tr>
<tr>
<td></td>
<td></td>
<td>0.5</td>
<td></td>
<td></td>
<td>&#x2212;2.3676</td>
</tr>
<tr>
<td>0.5</td>
<td>0.1</td>
<td>0.1</td>
<td>0.0</td>
<td>0.1</td>
<td>&#x2212;1.6174</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td>0.4</td>
<td></td>
<td>&#x2212;1.8586</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td>0.8</td>
<td></td>
<td>&#x2212;2.0732</td>
</tr>
<tr>
<td>0.5</td>
<td>0.1</td>
<td>0.1</td>
<td>0.2</td>
<td>0.0</td>
<td>&#x2212;1.8694</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.1</td>
<td>&#x2212;1.7420</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.2</td>
<td>&#x2212;1.5913</td>
</tr>
</tbody>
</table>
</table-wrap><table-wrap id="table-3">
<label>Table 3</label>
<caption>
<title>Analyzing the effects of several factors on Nusselt number by considering <inline-formula id="ieqn-119"><mml:math id="mml-ieqn-119"><mml:mi>K</mml:mi><mml:mo>=</mml:mo><mml:mi>L</mml:mi><mml:mi>e</mml:mi><mml:mo>=</mml:mo><mml:mi>P</mml:mi><mml:mi>e</mml:mi><mml:mo>=</mml:mo><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>2</mml:mn></mml:msub><mml:mo>=</mml:mo><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>3</mml:mn></mml:msub><mml:mo>=</mml:mo><mml:mn>0.1</mml:mn></mml:math></inline-formula>, <inline-formula id="ieqn-120"><mml:math id="mml-ieqn-120"><mml:mi>&#x03B1;</mml:mi><mml:mo>=</mml:mo><mml:mi>&#x03B4;</mml:mi><mml:mo>=</mml:mo><mml:mi mathvariant="normal">&#x03A9;</mml:mi><mml:mo>=</mml:mo><mml:mn>0.2</mml:mn></mml:math></inline-formula>, <inline-formula id="ieqn-121"><mml:math id="mml-ieqn-121"><mml:mi>&#x03B1;</mml:mi><mml:mo>=</mml:mo><mml:mn>0.5</mml:mn></mml:math></inline-formula>, <inline-formula id="ieqn-122"><mml:math id="mml-ieqn-122"><mml:mi>L</mml:mi><mml:mi>b</mml:mi><mml:mo>=</mml:mo><mml:mn>1</mml:mn></mml:math></inline-formula></title>
</caption>
<table frame="hsides">
<colgroup>
<col/>
<col/>
<col/>
<col/>
<col/>
<col/>
<col/>
<col/>
<col/>
<col/>
</colgroup>
<thead>
<tr>
<th><italic>M</italic></th>
<th><inline-formula id="ieqn-123"><mml:math id="mml-ieqn-123"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-124"><mml:math id="mml-ieqn-124"><mml:mi>&#x03B5;</mml:mi></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-125"><mml:math id="mml-ieqn-125"><mml:mi>P</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-126"><mml:math id="mml-ieqn-126"><mml:mi>E</mml:mi><mml:mi>c</mml:mi></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-127"><mml:math id="mml-ieqn-127"><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-128"><mml:math id="mml-ieqn-128"><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-129"><mml:math id="mml-ieqn-129"><mml:mi>&#x03B3;</mml:mi></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-130"><mml:math id="mml-ieqn-130"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-131"><mml:math id="mml-ieqn-131"><mml:mi>N</mml:mi><mml:msub><mml:mi>u</mml:mi><mml:mrow><mml:mi>x</mml:mi></mml:mrow></mml:msub><mml:msup><mml:mrow><mml:msub><mml:mi>R</mml:mi><mml:mrow><mml:mi>e</mml:mi></mml:mrow></mml:msub><mml:mi>x</mml:mi></mml:mrow><mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mn>1</mml:mn><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup></mml:math></inline-formula></th>
</tr>
</thead>
<tbody>
<tr>
<td>0.1</td>
<td>0.1</td>
<td>0.2</td>
<td>6</td>
<td>0.2</td>
<td>0.2</td>
<td>0.2</td>
<td>0.1</td>
<td>0.1</td>
<td>0.0571</td>
</tr>
<tr>
<td>0.5</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0413</td>
</tr>
<tr>
<td>0.9</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0255</td>
</tr>
<tr>
<td>0.1</td>
<td>0.1</td>
<td>0.2</td>
<td>6</td>
<td>0.2</td>
<td>0.2</td>
<td>0.2</td>
<td>0.1</td>
<td>0.1</td>
<td>0.0555</td>
</tr>
<tr>
<td></td>
<td>0.3</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0703</td>
</tr>
<tr>
<td></td>
<td>0.5</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0820</td>
</tr>
<tr>
<td>0.1</td>
<td>0.1</td>
<td>0.2</td>
<td>6</td>
<td>0.2</td>
<td>0.2</td>
<td>0.2</td>
<td>0.1</td>
<td>0.1</td>
<td>0.0571</td>
</tr>
<tr>
<td></td>
<td></td>
<td>0.5</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0589</td>
</tr>
<tr>
<td></td>
<td></td>
<td>0.8</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0597</td>
</tr>
<tr>
<td>0.1</td>
<td>0.1</td>
<td>0.2</td>
<td>6</td>
<td>0.2</td>
<td>0.2</td>
<td>0.2</td>
<td>0.1</td>
<td>0.1</td>
<td>0.0571</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td>7</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0555</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td>8</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0538</td>
</tr>
<tr>
<td>0.1</td>
<td>0.1</td>
<td>0.2</td>
<td>6</td>
<td>0.2</td>
<td>0.2</td>
<td>0.2</td>
<td>0.1</td>
<td>0.1</td>
<td>0.0571</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.3</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0345</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.4</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0065</td>
</tr>
<tr>
<td>0.1</td>
<td>0.1</td>
<td>0.2</td>
<td>6</td>
<td>0.2</td>
<td>0.2</td>
<td>0.2</td>
<td>0.1</td>
<td>0.1</td>
<td>0.0571</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.5</td>
<td></td>
<td></td>
<td></td>
<td>0.0543</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.8</td>
<td></td>
<td></td>
<td></td>
<td>0.0511</td>
</tr>
<tr>
<td>0.1</td>
<td>0.1</td>
<td>0.2</td>
<td>6</td>
<td>0.2</td>
<td>0.2</td>
<td>0.2</td>
<td>0.1</td>
<td>0.1</td>
<td>0.0571</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.5</td>
<td></td>
<td></td>
<td>0.0536</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.8</td>
<td></td>
<td></td>
<td>0.0493</td>
</tr>
<tr>
<td>0.1</td>
<td>0.1</td>
<td>0.2</td>
<td>6</td>
<td>0.2</td>
<td>0.2</td>
<td>0.2</td>
<td>0.0</td>
<td>0.1</td>
<td>0.0641</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.1</td>
<td></td>
<td>0.0571</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.15</td>
<td></td>
<td>0.0457</td>
</tr>
<tr>
<td>0.1</td>
<td>0.1</td>
<td>0.2</td>
<td>6</td>
<td>0.2</td>
<td>0.2</td>
<td>0.2</td>
<td>0.1</td>
<td>0.1</td>
<td>0.0571</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.5</td>
<td>0.1979</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.9</td>
<td>0.2650</td>
</tr>
</tbody>
</table>
</table-wrap><table-wrap id="table-4">
<label>Table 4</label>
<caption>
<title>Analyzing the effects of several factors on the Sherwood number by considering <inline-formula id="ieqn-132"><mml:math id="mml-ieqn-132"><mml:mi>K</mml:mi><mml:mo>=</mml:mo><mml:mi>M</mml:mi><mml:mo>=</mml:mo><mml:mi>&#x03BB;</mml:mi><mml:mi>&#x03B3;</mml:mi><mml:mo>=</mml:mo><mml:mi>P</mml:mi><mml:mi>e</mml:mi><mml:mo>=</mml:mo><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>3</mml:mn></mml:msub><mml:mo>=</mml:mo><mml:mn>0.1</mml:mn></mml:math></inline-formula>, <inline-formula id="ieqn-133"><mml:math id="mml-ieqn-133"><mml:mi>&#x03B4;</mml:mi><mml:mo>=</mml:mo><mml:mi>&#x03B5;</mml:mi><mml:mo>=</mml:mo><mml:mi>E</mml:mi><mml:mi>c</mml:mi><mml:mo>=</mml:mo><mml:mi mathvariant="normal">&#x03A9;</mml:mi><mml:mo>=</mml:mo><mml:mn>0.2</mml:mn></mml:math></inline-formula>, <inline-formula id="ieqn-134"><mml:math id="mml-ieqn-134"><mml:mi>&#x03B1;</mml:mi><mml:mo>=</mml:mo><mml:mn>0.5</mml:mn></mml:math></inline-formula>, <inline-formula id="ieqn-135"><mml:math id="mml-ieqn-135"><mml:mi>L</mml:mi><mml:mi>b</mml:mi><mml:mo>=</mml:mo><mml:mn>1</mml:mn></mml:math></inline-formula></title>
</caption>
<table frame="hsides">
<colgroup>
<col align="left"/>
<col align="left"/>
<col align="left"/>
<col align="left"/>
<col align="left"/>
<col align="left"/>
<col align="left"/>
</colgroup>
<thead>
<tr>
<th>Pr</th>
<th><inline-formula id="ieqn-136"><mml:math id="mml-ieqn-136"><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-137"><mml:math id="mml-ieqn-137"><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-138"><mml:math id="mml-ieqn-138"><mml:mi>L</mml:mi><mml:mi>e</mml:mi></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-139"><mml:math id="mml-ieqn-139"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-140"><mml:math id="mml-ieqn-140"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>2</mml:mn></mml:msub></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-141"><mml:math id="mml-ieqn-141"><mml:mi>S</mml:mi><mml:msub><mml:mi>h</mml:mi><mml:mrow><mml:mi>x</mml:mi></mml:mrow></mml:msub><mml:msup><mml:mrow><mml:msub><mml:mi>R</mml:mi><mml:mrow><mml:mi>e</mml:mi></mml:mrow></mml:msub><mml:mi>x</mml:mi></mml:mrow><mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mn>1</mml:mn><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup></mml:math></inline-formula></th>
</tr>
</thead>
<tbody>
<tr>
<td>6</td>
<td>0.2</td>
<td>0.2</td>
<td>0.1</td>
<td>0.1</td>
<td>0.1</td>
<td>0.0864</td>
</tr>
<tr>
<td>7</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0903</td>
</tr>
<tr>
<td>8</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0935</td>
</tr>
<tr>
<td>6</td>
<td>0.2</td>
<td>0.2</td>
<td>0.1</td>
<td>0.1</td>
<td>0.1</td>
<td>0.0864</td>
</tr>
<tr>
<td></td>
<td>0.5</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0832</td>
</tr>
<tr>
<td></td>
<td>0.8</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0824</td>
</tr>
<tr>
<td>6</td>
<td>0.2</td>
<td>0.2</td>
<td>0.1</td>
<td>0.1</td>
<td>0.1</td>
<td>0.0864</td>
</tr>
<tr>
<td></td>
<td></td>
<td>0.5</td>
<td></td>
<td></td>
<td></td>
<td>0.0904</td>
</tr>
<tr>
<td></td>
<td></td>
<td>0.8</td>
<td></td>
<td></td>
<td></td>
<td>0.0950</td>
</tr>
<tr>
<td>6</td>
<td>0.2</td>
<td>0.2</td>
<td>0.1</td>
<td>0.1</td>
<td>0.1</td>
<td>0.0864</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td>0.2</td>
<td></td>
<td></td>
<td>0.0953</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td>0.3</td>
<td></td>
<td></td>
<td>0.0986</td>
</tr>
<tr>
<td>6</td>
<td>0.2</td>
<td>0.2</td>
<td>0.1</td>
<td>0.1</td>
<td>0.1</td>
<td>0.0864</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.5</td>
<td></td>
<td>0.0655</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.9</td>
<td></td>
<td>0.0558</td>
</tr>
<tr>
<td>6</td>
<td>0.2</td>
<td>0.2</td>
<td>0.1</td>
<td>0.1</td>
<td>0.1</td>
<td>0.0864</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.5</td>
<td>0.2455</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.9</td>
<td>0.3087</td>
</tr>
</tbody>
</table>
</table-wrap><table-wrap id="table-5">
<label>Table 5</label>
<caption>
<title>Analyzing the effects of several factors on the density number by considering <inline-formula id="ieqn-142"><mml:math id="mml-ieqn-142"><mml:mi>K</mml:mi><mml:mo>=</mml:mo><mml:mi>&#x03B3;</mml:mi><mml:mo>=</mml:mo><mml:mi>L</mml:mi><mml:mi>e</mml:mi><mml:mo>=</mml:mo><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub><mml:mo>=</mml:mo><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>2</mml:mn></mml:msub><mml:mo>=</mml:mo><mml:mn>0.1</mml:mn><mml:mo>,</mml:mo></mml:math></inline-formula> <inline-formula id="ieqn-143"><mml:math id="mml-ieqn-143"><mml:mi>&#x03B4;</mml:mi><mml:mo>=</mml:mo><mml:mi>&#x03B5;</mml:mi><mml:mo>=</mml:mo><mml:mi>E</mml:mi><mml:mi>c</mml:mi><mml:mo>=</mml:mo><mml:mi>N</mml:mi><mml:mi>b</mml:mi><mml:mo>=</mml:mo><mml:mi>N</mml:mi><mml:mi>t</mml:mi><mml:mo>=</mml:mo><mml:mn>0.2</mml:mn><mml:mo>,</mml:mo></mml:math></inline-formula> <inline-formula id="ieqn-144"><mml:math id="mml-ieqn-144"><mml:mi>&#x03B1;</mml:mi><mml:mo>=</mml:mo><mml:mn>0.5</mml:mn><mml:mo>,</mml:mo></mml:math></inline-formula> <italic>Pr</italic> &#x003D; 6, <inline-formula id="ieqn-145"><mml:math id="mml-ieqn-145"><mml:mi>L</mml:mi><mml:mi>b</mml:mi><mml:mo>=</mml:mo><mml:mn>1</mml:mn></mml:math></inline-formula><break/></title>
</caption>
<table frame="hsides">
<colgroup>
<col align="left"/>
<col align="left"/>
<col align="left"/>
<col align="left"/>
<col align="left"/>
<col align="left"/>
<col align="left"/>
</colgroup>
<thead>
<tr>
<th>M</th>
<th><inline-formula id="ieqn-146"><mml:math id="mml-ieqn-146"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-147"><mml:math id="mml-ieqn-147"><mml:mi>L</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-148"><mml:math id="mml-ieqn-148"><mml:mi>P</mml:mi><mml:mi>e</mml:mi></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-149"><mml:math id="mml-ieqn-149"><mml:mi mathvariant="normal">&#x03A9;</mml:mi></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-150"><mml:math id="mml-ieqn-150"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>3</mml:mn></mml:msub></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-151"><mml:math id="mml-ieqn-151"><mml:mi>D</mml:mi><mml:msub><mml:mi>n</mml:mi><mml:mrow><mml:mi>x</mml:mi></mml:mrow></mml:msub><mml:msup><mml:mrow><mml:msub><mml:mi>R</mml:mi><mml:mrow><mml:mi>e</mml:mi></mml:mrow></mml:msub><mml:mi>x</mml:mi></mml:mrow><mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mn>1</mml:mn><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup></mml:math></inline-formula></th>
</tr>
</thead>
<tbody>
<tr>
<td>0.1</td>
<td>0.1</td>
<td>1</td>
<td>0.1</td>
<td>0.2</td>
<td>0.1</td>
<td>0.0856</td>
</tr>
<tr>
<td>0.5</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0851</td>
</tr>
<tr>
<td>0.9</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0847</td>
</tr>
<tr>
<td>0.1</td>
<td>0.0</td>
<td>1</td>
<td>0.1</td>
<td>0.2</td>
<td>0.1</td>
<td>0.0848</td>
</tr>
<tr>
<td></td>
<td>0.1</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0856</td>
</tr>
<tr>
<td></td>
<td>0.2</td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.0862</td>
</tr>
<tr>
<td>0.1</td>
<td>0.1</td>
<td>1</td>
<td>0.1</td>
<td>0.2</td>
<td>0.1</td>
<td>0.0856</td>
</tr>
<tr>
<td></td>
<td></td>
<td>2</td>
<td></td>
<td></td>
<td></td>
<td>0.0902</td>
</tr>
<tr>
<td></td>
<td></td>
<td>3</td>
<td></td>
<td></td>
<td></td>
<td>0.0922</td>
</tr>
<tr>
<td>0.1</td>
<td>0.1</td>
<td>1</td>
<td>0.1</td>
<td>0.2</td>
<td>0.1</td>
<td>0.0856</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td>0.3</td>
<td></td>
<td></td>
<td>0.0868</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td>0.5</td>
<td></td>
<td></td>
<td>0.0880</td>
</tr>
<tr>
<td>0.1</td>
<td>0.1</td>
<td>1</td>
<td>0.1</td>
<td>0.1</td>
<td>0.1</td>
<td>0.0854</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.3</td>
<td></td>
<td>0.0857</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.5</td>
<td></td>
<td>0.0861</td>
</tr>
<tr>
<td>0.1</td>
<td>0.1</td>
<td>1</td>
<td>0.1</td>
<td>0.2</td>
<td>0.1</td>
<td>0.0856</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.3</td>
<td>0.1981</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td></td>
<td></td>
<td>0.5</td>
<td>0.2687</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>The convective heat transfer at a solid-fluid interface is represented by the local Nusselt number. It exhibits a decreasing trend with <italic>M</italic> the magnetic parameter, <inline-formula id="ieqn-152"><mml:math id="mml-ieqn-152"><mml:mi>E</mml:mi><mml:mi>c</mml:mi></mml:math></inline-formula> the Eckert number, <inline-formula id="ieqn-153"><mml:math id="mml-ieqn-153"><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula> the Brownian motion parameter, <inline-formula id="ieqn-154"><mml:math id="mml-ieqn-154"><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:math></inline-formula> the thermophoresis parameter, and the local heat source/sink parameter <inline-formula id="ieqn-155"><mml:math id="mml-ieqn-155"><mml:mi>&#x03B3;</mml:mi></mml:math></inline-formula> but rises with the ratio parameter <inline-formula id="ieqn-156"><mml:math id="mml-ieqn-156"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula>, thermal conductivity parameter <inline-formula id="ieqn-157"><mml:math id="mml-ieqn-157"><mml:mi>&#x03B5;</mml:mi></mml:math></inline-formula> and thermal number <inline-formula id="ieqn-158"><mml:math id="mml-ieqn-158"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub></mml:math></inline-formula>. Furthermore, with an increase in the Prandtl number <inline-formula id="ieqn-159"><mml:math id="mml-ieqn-159"><mml:mi>P</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula>, we have seen a notable improvement of about 6% in fluid thermal conductivity.</p>
<p>The convective mass transfer is represented by the local Sherwood number. For local Sherwood number, it is observed that it rises with <inline-formula id="ieqn-160"><mml:math id="mml-ieqn-160"><mml:mi>P</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula> the Prandtl number, <inline-formula id="ieqn-161"><mml:math id="mml-ieqn-161"><mml:mi>L</mml:mi><mml:mi>e</mml:mi></mml:math></inline-formula> the Lewis number, <inline-formula id="ieqn-162"><mml:math id="mml-ieqn-162"><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:math></inline-formula> the thermophoresis parameter, and the concentration Biot number, but drops with <inline-formula id="ieqn-163"><mml:math id="mml-ieqn-163"><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula> and <inline-formula id="ieqn-164"><mml:math id="mml-ieqn-164"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub></mml:math></inline-formula>.</p>
<p>Finally, the local density number describes how the density of mobile microorganisms varies in the fluid. The behavior of this parameter has ramifications for environmental and biotechnological applications and is essential to understanding biological convection processes. It grows with <inline-formula id="ieqn-165"><mml:math id="mml-ieqn-165"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-166"><mml:math id="mml-ieqn-166"><mml:mi>L</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-167"><mml:math id="mml-ieqn-167"><mml:mi>P</mml:mi><mml:mi>e</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-168"><mml:math id="mml-ieqn-168"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>3</mml:mn></mml:msub></mml:math></inline-formula>, and <inline-formula id="ieqn-169"><mml:math id="mml-ieqn-169"><mml:mi>&#x03C9;</mml:mi></mml:math></inline-formula>, but decreases with the magnetic number <italic>M</italic>. So, the diffusibility of microorganisms tends to increase for all the parameters considered in the study, except for the magnetic parameter <italic>M</italic>.</p>
<p><xref ref-type="fig" rid="fig-1">Fig. 1</xref> presents the diagrammatic depiction of the flow model. <xref ref-type="fig" rid="fig-2">Figs. 2</xref>&#x2013;<xref ref-type="fig" rid="fig-5">5</xref> present the velocity profile under varying conditions of the viscosity parameter <inline-formula id="ieqn-170"><mml:math id="mml-ieqn-170"><mml:mi>&#x03B1;</mml:mi></mml:math></inline-formula>, magnetic number <italic>M</italic>, local Darcy number <inline-formula id="ieqn-171"><mml:math id="mml-ieqn-171"><mml:mi>&#x03B4;</mml:mi></mml:math></inline-formula>, and ratio parameter <inline-formula id="ieqn-172"><mml:math id="mml-ieqn-172"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula>. Except for <inline-formula id="ieqn-173"><mml:math id="mml-ieqn-173"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula>, it is shown that the fluid velocity drops as <inline-formula id="ieqn-174"><mml:math id="mml-ieqn-174"><mml:mi>&#x03B1;</mml:mi></mml:math></inline-formula>, <italic>M</italic>, and <inline-formula id="ieqn-175"><mml:math id="mml-ieqn-175"><mml:mi>&#x03B4;</mml:mi></mml:math></inline-formula> rise. On the other hand, a rise in the value of lambda causes an increase in fluid velocity.</p>
<fig id="fig-1">
<label>Figure 1</label>
<caption>
<title>A diagrammatic depiction of the flow model</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-1.tif"/>
</fig><fig id="fig-2">
<label>Figure 2</label>
<caption>
<title><inline-formula id="ieqn-176"><mml:math id="mml-ieqn-176"><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mi>&#x03B7;</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula> against <inline-formula id="ieqn-177"><mml:math id="mml-ieqn-177"><mml:mi>&#x03B1;</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-2.tif"/>
</fig><fig id="fig-3">
<label>Figure 3</label>
<caption>
<title><inline-formula id="ieqn-178"><mml:math id="mml-ieqn-178"><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mi>&#x03B7;</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula> against <italic>M</italic></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-3.tif"/>
</fig><fig id="fig-4">
<label>Figure 4</label>
<caption>
<title><inline-formula id="ieqn-179"><mml:math id="mml-ieqn-179"><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mi>&#x03B7;</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula> against <inline-formula id="ieqn-180"><mml:math id="mml-ieqn-180"><mml:mi>&#x03B4;</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-4.tif"/>
</fig><fig id="fig-5">
<label>Figure 5</label>
<caption>
<title><inline-formula id="ieqn-181"><mml:math id="mml-ieqn-181"><mml:msup><mml:mi>f</mml:mi><mml:mrow><mml:mo>&#x2032;</mml:mo></mml:mrow></mml:msup><mml:mo stretchy="false">(</mml:mo><mml:mi>&#x03B7;</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula> against <inline-formula id="ieqn-182"><mml:math id="mml-ieqn-182"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-5.tif"/>
</fig>
<p>The temperature profile is shown in <xref ref-type="fig" rid="fig-6">Figs. 6</xref>&#x2013;<xref ref-type="fig" rid="fig-13">13</xref> by considering a range of values for the Prandtl number <inline-formula id="ieqn-183"><mml:math id="mml-ieqn-183"><mml:mi>P</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula>, the ratio parameter <inline-formula id="ieqn-184"><mml:math id="mml-ieqn-184"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula>, the thermal conductivity parameter <inline-formula id="ieqn-185"><mml:math id="mml-ieqn-185"><mml:mi>&#x03B5;</mml:mi></mml:math></inline-formula>, and the Eckert number <inline-formula id="ieqn-186"><mml:math id="mml-ieqn-186"><mml:mi>E</mml:mi><mml:mi>c</mml:mi></mml:math></inline-formula>, the Brownian motion parameter <inline-formula id="ieqn-187"><mml:math id="mml-ieqn-187"><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula>, the thermophoresis parameter <inline-formula id="ieqn-188"><mml:math id="mml-ieqn-188"><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:math></inline-formula>, the thermal number <inline-formula id="ieqn-189"><mml:math id="mml-ieqn-189"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub></mml:math></inline-formula>, and the magnetic number <italic>M</italic>. The temperature profile is affected by changes in the thermal conductivity parameter <inline-formula id="ieqn-190"><mml:math id="mml-ieqn-190"><mml:mi>&#x03B5;</mml:mi></mml:math></inline-formula>, as seen in <xref ref-type="fig" rid="fig-8">Fig. 8</xref>. It was discovered that increasing the thermal conductivity parameter gave greater heat to neighboring liquid particles. <xref ref-type="fig" rid="fig-9">Figs. 9</xref>&#x2013;<xref ref-type="fig" rid="fig-13">13</xref> depict the effect of the Eckert number <inline-formula id="ieqn-191"><mml:math id="mml-ieqn-191"><mml:mi>E</mml:mi><mml:mi>c</mml:mi></mml:math></inline-formula>, Brownian motion parameter <inline-formula id="ieqn-192"><mml:math id="mml-ieqn-192"><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula>, thermophoresis parameter <inline-formula id="ieqn-193"><mml:math id="mml-ieqn-193"><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:math></inline-formula>, thermal number <inline-formula id="ieqn-194"><mml:math id="mml-ieqn-194"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub></mml:math></inline-formula>, and magnetic number <italic>M</italic> on the temperature profile. The temperature profile grow as <inline-formula id="ieqn-195"><mml:math id="mml-ieqn-195"><mml:mi>E</mml:mi><mml:mi>c</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-196"><mml:math id="mml-ieqn-196"><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-197"><mml:math id="mml-ieqn-197"><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-198"><mml:math id="mml-ieqn-198"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub></mml:math></inline-formula>, and <italic>M</italic> increased.</p>
<fig id="fig-6">
<label>Figure 6</label>
<caption>
<title>Temperature profile against <inline-formula id="ieqn-199"><mml:math id="mml-ieqn-199"><mml:mi>P</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-6.tif"/>
</fig><fig id="fig-7">
<label>Figure 7</label>
<caption>
<title>Temperature profile against <inline-formula id="ieqn-200"><mml:math id="mml-ieqn-200"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-7.tif"/>
</fig><fig id="fig-8">
<label>Figure 8</label>
<caption>
<title>Temperature profile against <inline-formula id="ieqn-217"><mml:math id="mml-ieqn-217"><mml:mi>&#x03B5;</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-8.tif"/>
</fig><fig id="fig-9">
<label>Figure 9</label>
<caption>
<title>Temperature profile against <inline-formula id="ieqn-218"><mml:math id="mml-ieqn-218"><mml:mi>E</mml:mi><mml:mi>c</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-9.tif"/>
</fig><fig id="fig-10">
<label>Figure 10</label>
<caption>
<title>Temperature profile against <inline-formula id="ieqn-225"><mml:math id="mml-ieqn-225"><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-10.tif"/>
</fig><fig id="fig-11">
<label>Figure 11</label>
<caption>
<title>Temperature profile against <inline-formula id="ieqn-226"><mml:math id="mml-ieqn-226"><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-11.tif"/>
</fig><fig id="fig-12">
<label>Figure 12</label>
<caption>
<title>Temperature profile against <inline-formula id="ieqn-227"><mml:math id="mml-ieqn-227"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-12.tif"/>
</fig><fig id="fig-13">
<label>Figure 13</label>
<caption>
<title>Temperature profile against <italic>M</italic></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-13.tif"/>
</fig>
<p><xref ref-type="fig" rid="fig-14">Figs. 14</xref> to <xref ref-type="fig" rid="fig-19">19</xref> explore the concentration profile for various values of the Prandtl number <inline-formula id="ieqn-201"><mml:math id="mml-ieqn-201"><mml:mi>P</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula>, the thermophoresis parameters <inline-formula id="ieqn-202"><mml:math id="mml-ieqn-202"><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula>, the Brownian motion parameter <inline-formula id="ieqn-203"><mml:math id="mml-ieqn-203"><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:math></inline-formula>, the Lewis number <inline-formula id="ieqn-204"><mml:math id="mml-ieqn-204"><mml:mi>L</mml:mi><mml:mi>e</mml:mi></mml:math></inline-formula>, the thermal number <inline-formula id="ieqn-205"><mml:math id="mml-ieqn-205"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub></mml:math></inline-formula>, and the concentration Biot number <inline-formula id="ieqn-206"><mml:math id="mml-ieqn-206"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>2</mml:mn></mml:msub></mml:math></inline-formula>. In <xref ref-type="fig" rid="fig-14">Fig. 14</xref>, a decrease in the concentration field is observed when <inline-formula id="ieqn-207"><mml:math id="mml-ieqn-207"><mml:mi>P</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula> goes from <inline-formula id="ieqn-208"><mml:math id="mml-ieqn-208"><mml:mn>6</mml:mn></mml:math></inline-formula> to <inline-formula id="ieqn-209"><mml:math id="mml-ieqn-209"><mml:mn>8</mml:mn></mml:math></inline-formula>. <xref ref-type="fig" rid="fig-15">Fig. 15</xref> depicts the effect of the thermophoresis parameter <inline-formula id="ieqn-210"><mml:math id="mml-ieqn-210"><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula> on the concentration profile, demonstrating that the concentration profile decreases as <inline-formula id="ieqn-211"><mml:math id="mml-ieqn-211"><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula> increases. <xref ref-type="fig" rid="fig-16">Fig. 16</xref>, on the other hand, demonstrates that the concentration field grows in response to <inline-formula id="ieqn-212"><mml:math id="mml-ieqn-212"><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:math></inline-formula>. Changes in the Lewis number <inline-formula id="ieqn-213"><mml:math id="mml-ieqn-213"><mml:mi>L</mml:mi><mml:mi>e</mml:mi></mml:math></inline-formula> are shown to have an impact on the concentration profile in <xref ref-type="fig" rid="fig-17">Fig. 17</xref>. A drop in the concentration profile is shown to be accompanied by an increase in <inline-formula id="ieqn-214"><mml:math id="mml-ieqn-214"><mml:mi>L</mml:mi><mml:mi>e</mml:mi></mml:math></inline-formula>. Additionally, the thermal number <inline-formula id="ieqn-215"><mml:math id="mml-ieqn-215"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub></mml:math></inline-formula> and the concentration Biot number <inline-formula id="ieqn-216"><mml:math id="mml-ieqn-216"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>2</mml:mn></mml:msub></mml:math></inline-formula> vary for various parameter values, as shown in <xref ref-type="fig" rid="fig-18">Figs. 18</xref> and <xref ref-type="fig" rid="fig-19">19</xref>. The concentration boundary layer expands in both cases.</p>
<fig id="fig-14">
<label>Figure 14</label>
<caption>
<title>Concentration profile against <inline-formula id="ieqn-228"><mml:math id="mml-ieqn-228"><mml:mi>P</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-14.tif"/>
</fig><fig id="fig-15">
<label>Figure 15</label>
<caption>
<title>Concentration profile against <inline-formula id="ieqn-229"><mml:math id="mml-ieqn-229"><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-15.tif"/>
</fig><fig id="fig-16">
<label>Figure 16</label>
<caption>
<title>Concentration profile against <inline-formula id="ieqn-230"><mml:math id="mml-ieqn-230"><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-16.tif"/>
</fig><fig id="fig-17">
<label>Figure 17</label>
<caption>
<title>Concentration profile against <inline-formula id="ieqn-231"><mml:math id="mml-ieqn-231"><mml:mi>L</mml:mi><mml:mi>e</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-17.tif"/>
</fig><fig id="fig-18">
<label>Figure 18</label>
<caption>
<title>Concentration profile against <inline-formula id="ieqn-232"><mml:math id="mml-ieqn-232"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-18.tif"/>
</fig><fig id="fig-19">
<label>Figure 19</label>
<caption>
<title>Concentration profile against <inline-formula id="ieqn-233"><mml:math id="mml-ieqn-233"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>2</mml:mn></mml:msub></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-19.tif"/>
</fig>
<p><xref ref-type="fig" rid="fig-20">Figs. 20</xref> to <xref ref-type="fig" rid="fig-23">23</xref> show the microorganism profile for various values of the bio-convection Lewis number <inline-formula id="ieqn-219"><mml:math id="mml-ieqn-219"><mml:mi>L</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula>, concentration difference parameter <inline-formula id="ieqn-220"><mml:math id="mml-ieqn-220"><mml:mi mathvariant="normal">&#x03A9;</mml:mi></mml:math></inline-formula>, magnetic number <italic>M</italic>, and density number <inline-formula id="ieqn-221"><mml:math id="mml-ieqn-221"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>3</mml:mn></mml:msub></mml:math></inline-formula>. It is seen that the motile density profile falls for <inline-formula id="ieqn-222"><mml:math id="mml-ieqn-222"><mml:mi>L</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula> and <inline-formula id="ieqn-223"><mml:math id="mml-ieqn-223"><mml:mi mathvariant="normal">&#x03A9;</mml:mi></mml:math></inline-formula> but grows for all other parameters, showing that the diffusivity of microorganisms increases for <italic>M</italic> and <inline-formula id="ieqn-224"><mml:math id="mml-ieqn-224"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>3</mml:mn></mml:msub></mml:math></inline-formula>.</p>
<fig id="fig-20">
<label>Figure 20</label>
<caption>
<title>Microorganisms profile against <inline-formula id="ieqn-234"><mml:math id="mml-ieqn-234"><mml:mi>L</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-20.tif"/>
</fig><fig id="fig-21">
<label>Figure 21</label>
<caption>
<title>Microorganisms profile against <italic>M</italic></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-21.tif"/>
</fig><fig id="fig-22">
<label>Figure 22</label>
<caption>
<title>Microorganisms profile against <inline-formula id="ieqn-235"><mml:math id="mml-ieqn-235"><mml:mi mathvariant="normal">&#x03A9;</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-22.tif"/>
</fig><fig id="fig-23">
<label>Figure 23</label>
<caption>
<title>Microorganisms profile against <inline-formula id="ieqn-236"><mml:math id="mml-ieqn-236"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>3</mml:mn></mml:msub></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="FHMT_44587-fig-23.tif"/>
</fig>
<p>In summary, our numerical findings illuminate the intricate interactions between different factors in fluid dynamics, heat transfer, mass transfer, and microorganism dynamics. Engineering, environmental science, and biotechnology can all benefit from these discoveries. For better performance and efficiency, fluid systems can be designed and optimized using the observed trends and dependencies.</p>
<p>Our findings serve as the foundation for more advanced research in this subject. These fundamental ideas, we feel, are critical for building a comprehensive understanding of the phenomena under investigation. Future research can build on these foundations to investigate more complex scenarios and solve specific engineering problems.</p>
</sec>
<sec id="s5">
<label>5</label>
<title>Conclusion</title>
<p>This paper gives the following conclusions based on the analysis and discussion of the results after conducting study on the two-dimensional flow stagnates at <inline-formula id="ieqn-237"><mml:math id="mml-ieqn-237"><mml:mi>x</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:math></inline-formula> over an extended heated elastic sheet under radiative heat transfer with nonlinear characteristics, variable viscosity, and MHD in a porous medium. Moreover, we extend our analysis by considering convective boundary conditions and introducing the gyrotactic microorganisms equation to capture microorganism behavior influenced by fluid flow.
<list list-type="order">
<list-item><p>Various parameters such as <inline-formula id="ieqn-238"><mml:math id="mml-ieqn-238"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-239"><mml:math id="mml-ieqn-239"><mml:mi>&#x03B1;</mml:mi></mml:math></inline-formula>, <italic>K</italic>, <italic>M</italic>, and <inline-formula id="ieqn-240"><mml:math id="mml-ieqn-240"><mml:mi>&#x03B4;</mml:mi></mml:math></inline-formula> influence the skin friction coefficient. An increase in <inline-formula id="ieqn-241"><mml:math id="mml-ieqn-241"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula> causes the fluid speed to decrease, whereas an increase in <inline-formula id="ieqn-242"><mml:math id="mml-ieqn-242"><mml:mi>&#x03B1;</mml:mi></mml:math></inline-formula>, <italic>K</italic>, <italic>M</italic>, or <inline-formula id="ieqn-243"><mml:math id="mml-ieqn-243"><mml:mi>&#x03B4;</mml:mi></mml:math></inline-formula> causes it to increase. Our investigations reveal that, contingent upon the magnetic parameter M, the presence of a porous medium leads to a substantial enhancement in fluid velocity, ranging between approximately 25% and 45%.</p></list-item>
<list-item><p>Fluid temperature is affected by parameters such as <italic>M</italic>, <inline-formula id="ieqn-244"><mml:math id="mml-ieqn-244"><mml:mi>E</mml:mi><mml:mi>c</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-245"><mml:math id="mml-ieqn-245"><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-246"><mml:math id="mml-ieqn-246"><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-247"><mml:math id="mml-ieqn-247"><mml:mi>&#x03B3;</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-248"><mml:math id="mml-ieqn-248"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-249"><mml:math id="mml-ieqn-249"><mml:mi>P</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-250"><mml:math id="mml-ieqn-250"><mml:mi>&#x03B5;</mml:mi></mml:math></inline-formula>, and <inline-formula id="ieqn-251"><mml:math id="mml-ieqn-251"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub></mml:math></inline-formula>. An increase in <italic>M</italic>, <inline-formula id="ieqn-252"><mml:math id="mml-ieqn-252"><mml:mi>E</mml:mi><mml:mi>c</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-253"><mml:math id="mml-ieqn-253"><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-254"><mml:math id="mml-ieqn-254"><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:math></inline-formula>, or <inline-formula id="ieqn-255"><mml:math id="mml-ieqn-255"><mml:mi>&#x03B3;</mml:mi></mml:math></inline-formula> causes a reduction in fluid temperature, whereas a rise in <inline-formula id="ieqn-256"><mml:math id="mml-ieqn-256"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-257"><mml:math id="mml-ieqn-257"><mml:mi>&#x03B5;</mml:mi></mml:math></inline-formula>, or <inline-formula id="ieqn-258"><mml:math id="mml-ieqn-258"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub></mml:math></inline-formula> causes an increase. An increase in the Prandtl number (Pr) results in a noticeable improvement of around 6% in fluid thermal conductivity.</p></list-item>
<list-item><p>The concentration boundary layer thickness is determined by parameters such as <inline-formula id="ieqn-259"><mml:math id="mml-ieqn-259"><mml:mi>P</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-260"><mml:math id="mml-ieqn-260"><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-261"><mml:math id="mml-ieqn-261"><mml:mi>L</mml:mi><mml:mi>e</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-262"><mml:math id="mml-ieqn-262"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>2</mml:mn></mml:msub></mml:math></inline-formula>, <inline-formula id="ieqn-263"><mml:math id="mml-ieqn-263"><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:math></inline-formula>, and <inline-formula id="ieqn-264"><mml:math id="mml-ieqn-264"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub></mml:math></inline-formula>. An increase in <inline-formula id="ieqn-265"><mml:math id="mml-ieqn-265"><mml:mi>P</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-266"><mml:math id="mml-ieqn-266"><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-267"><mml:math id="mml-ieqn-267"><mml:mi>L</mml:mi><mml:mi>e</mml:mi></mml:math></inline-formula>, or <inline-formula id="ieqn-268"><mml:math id="mml-ieqn-268"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>2</mml:mn></mml:msub></mml:math></inline-formula> causes the concentration boundary layer thickness to grow, whereas an increase in <inline-formula id="ieqn-269"><mml:math id="mml-ieqn-269"><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula> or <inline-formula id="ieqn-270"><mml:math id="mml-ieqn-270"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>1</mml:mn></mml:msub></mml:math></inline-formula> causes it to drop.</p></list-item>
<list-item><p>The local density number is influenced by parameters such as <inline-formula id="ieqn-271"><mml:math id="mml-ieqn-271"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-272"><mml:math id="mml-ieqn-272"><mml:mi>L</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-273"><mml:math id="mml-ieqn-273"><mml:mi>P</mml:mi><mml:mi>e</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-274"><mml:math id="mml-ieqn-274"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>3</mml:mn></mml:msub></mml:math></inline-formula>, <inline-formula id="ieqn-275"><mml:math id="mml-ieqn-275"><mml:mi mathvariant="normal">&#x03A9;</mml:mi></mml:math></inline-formula>, and <italic>M</italic>. An increase in <inline-formula id="ieqn-276"><mml:math id="mml-ieqn-276"><mml:mi>&#x03BB;</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-277"><mml:math id="mml-ieqn-277"><mml:mi>L</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-278"><mml:math id="mml-ieqn-278"><mml:mi>P</mml:mi><mml:mi>e</mml:mi></mml:math></inline-formula>, <inline-formula id="ieqn-279"><mml:math id="mml-ieqn-279"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>3</mml:mn></mml:msub></mml:math></inline-formula>, or <inline-formula id="ieqn-280"><mml:math id="mml-ieqn-280"><mml:mi mathvariant="normal">&#x03A9;</mml:mi></mml:math></inline-formula> leads to an increase in the local density number, while an increase in <italic>M</italic> results in a decrease.</p></list-item>
</list></p>
<p>These findings provide insight into the behavior of fluid flow under various physical conditions and can be used to optimize industrial processes. The mathematical modeling approach used in this study can be applied to other related problems to gain a better understanding of fluid dynamics in various industrial applications.</p>
</sec>
</body>
<back>
<glossary content-type="abbreviations" id="glossary-1">
<title>Nomenclature</title>
<def-list>
<def-item>
<term><inline-formula id="ieqn-3"><mml:math id="mml-ieqn-3"><mml:mi>u</mml:mi><mml:mo>,</mml:mo><mml:mi>v</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mi>m</mml:mi><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mi>s</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula></term>
<def>
<p>Velocity component along <inline-formula id="ieqn-4"><mml:math id="mml-ieqn-4"><mml:mo stretchy="false">(</mml:mo><mml:mi>x</mml:mi><mml:mo>,</mml:mo><mml:mi>y</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-5"><mml:math id="mml-ieqn-5"><mml:msub><mml:mi>B</mml:mi><mml:mn>0</mml:mn></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mi>A</mml:mi><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mi>M</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula></term>
<def>
<p>Constant magnetic field</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-6"><mml:math id="mml-ieqn-6"><mml:msub><mml:mi>&#x03C1;</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mi>K</mml:mi><mml:mi>g</mml:mi><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:msup><mml:mi>m</mml:mi><mml:mn>3</mml:mn></mml:msup><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula></term>
<def>
<p>Density of fluid</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-7"><mml:math id="mml-ieqn-7"><mml:msub><mml:mi>&#x03BD;</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:msup><mml:mi>m</mml:mi><mml:mn>2</mml:mn></mml:msup><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mi>s</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula></term>
<def>
<p>Kinematic viscosity</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-8"><mml:math id="mml-ieqn-8"><mml:msub><mml:mi>u</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mi>m</mml:mi><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mi>s</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula></term>
<def>
<p>Free stream velocity</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-9"><mml:math id="mml-ieqn-9"><mml:msub><mml:mi>&#x03C3;</mml:mi><mml:mi>e</mml:mi></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mi>S</mml:mi><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mi>m</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula></term>
<def>
<p>Electrical conductivity</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-10"><mml:math id="mml-ieqn-10"><mml:msub><mml:mi>k</mml:mi><mml:mn>0</mml:mn></mml:msub></mml:math></inline-formula></term>
<def>
<p>Viscoelastic parameter</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-11"><mml:math id="mml-ieqn-11"><mml:msub><mml:mi>T</mml:mi><mml:mi>f</mml:mi></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mi>K</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula></term>
<def>
<p>Temperature of FLuid</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-12"><mml:math id="mml-ieqn-12"><mml:msub><mml:mi>Q</mml:mi><mml:mn>0</mml:mn></mml:msub></mml:math></inline-formula></term>
<def>
<p>Heat source parameter</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-13"><mml:math id="mml-ieqn-13"><mml:msub><mml:mi>D</mml:mi><mml:mi>B</mml:mi></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:msup><mml:mi>m</mml:mi><mml:mn>2</mml:mn></mml:msup><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mi>s</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula></term>
<def>
<p>Browninan diffusion</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-14"><mml:math id="mml-ieqn-14"><mml:mi>T</mml:mi><mml:mo>,</mml:mo><mml:mi>C</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mi>K</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula></term>
<def>
<p>Temperature and concentration</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-15"><mml:math id="mml-ieqn-15"><mml:msub><mml:mi>T</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mi>K</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula></term>
<def>
<p>Free stream temperature</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-16"><mml:math id="mml-ieqn-16"><mml:msub><mml:mi>&#x03B3;</mml:mi><mml:mn>2</mml:mn></mml:msub></mml:math></inline-formula></term>
<def>
<p>Concentration biot number</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-17"><mml:math id="mml-ieqn-17"><mml:mi>L</mml:mi><mml:mi>e</mml:mi></mml:math></inline-formula></term>
<def>
<p>Lewis number</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-18"><mml:math id="mml-ieqn-18"><mml:msub><mml:mi>D</mml:mi><mml:mi>n</mml:mi></mml:msub></mml:math></inline-formula></term>
<def>
<p>Microorganisms diffususion</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-19"><mml:math id="mml-ieqn-19"><mml:msub><mml:mi>h</mml:mi><mml:mn>3</mml:mn></mml:msub></mml:math></inline-formula></term>
<def>
<p>Microorganisms transfer coefficients</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-20"><mml:math id="mml-ieqn-20"><mml:msub><mml:mi>N</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub></mml:math></inline-formula></term>
<def>
<p>Ambient microorganism concentration</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-21"><mml:math id="mml-ieqn-21"><mml:mi>P</mml:mi><mml:mi>e</mml:mi></mml:math></inline-formula></term>
<def>
<p>Peclet number</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-22"><mml:math id="mml-ieqn-22"><mml:mi>k</mml:mi><mml:mo stretchy="false">(</mml:mo><mml:mi>W</mml:mi><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mi>m</mml:mi><mml:mi>K</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula></term>
<def>
<p>Thermal conductivity</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-23"><mml:math id="mml-ieqn-23"><mml:msub><mml:mi>D</mml:mi><mml:mrow><mml:mi>T</mml:mi></mml:mrow></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:msup><mml:mi>m</mml:mi><mml:mn>2</mml:mn></mml:msup><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mi>s</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula></term>
<def>
<p>Thermophoretic diffusion coefficients</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-24"><mml:math id="mml-ieqn-24"><mml:msub><mml:mi>C</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mi>m</mml:mi><mml:mi>o</mml:mi><mml:mi>l</mml:mi><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:msup><mml:mi>m</mml:mi><mml:mn>3</mml:mn></mml:msup><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula></term>
<def>
<p>The ambient fluid concentration</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-25"><mml:math id="mml-ieqn-25"><mml:msub><mml:mi>P</mml:mi><mml:mrow><mml:mi>r</mml:mi></mml:mrow></mml:msub></mml:math></inline-formula></term>
<def>
<p>The ambient Prandtl number</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-26"><mml:math id="mml-ieqn-26"><mml:mi>N</mml:mi><mml:mi>t</mml:mi></mml:math></inline-formula></term>
<def>
<p>Thermophoresis number</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-27"><mml:math id="mml-ieqn-27"><mml:mi>N</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula></term>
<def>
<p>Brownian motion parameter</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-28"><mml:math id="mml-ieqn-28"><mml:mi>N</mml:mi><mml:msub><mml:mi>u</mml:mi><mml:mi>x</mml:mi></mml:msub></mml:math></inline-formula></term>
<def>
<p>Nusselt parameter</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-29"><mml:math id="mml-ieqn-29"><mml:mi>S</mml:mi><mml:msub><mml:mi>h</mml:mi><mml:mi>x</mml:mi></mml:msub></mml:math></inline-formula></term>
<def>
<p>Sherwood parameter</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-30"><mml:math id="mml-ieqn-30"><mml:mi>D</mml:mi><mml:msub><mml:mi>n</mml:mi><mml:mi>x</mml:mi></mml:msub></mml:math></inline-formula></term>
<def>
<p>Density parameter</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-31"><mml:math id="mml-ieqn-31"><mml:msub><mml:mi>W</mml:mi><mml:mi>c</mml:mi></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:mi>m</mml:mi><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mi>s</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula></term>
<def>
<p>Maximum cell swimming speed</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-32"><mml:math id="mml-ieqn-32"><mml:msub><mml:mi>D</mml:mi><mml:mi>m</mml:mi></mml:msub><mml:mo stretchy="false">(</mml:mo><mml:msup><mml:mi>m</mml:mi><mml:mn>2</mml:mn></mml:msup><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mi>s</mml:mi><mml:mo stretchy="false">)</mml:mo></mml:math></inline-formula></term>
<def>
<p>Diffusivity of microorganism</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-33"><mml:math id="mml-ieqn-33"><mml:msub><mml:mi>N</mml:mi><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:msub></mml:math></inline-formula></term>
<def>
<p>Ambient microorganism concentration</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-34"><mml:math id="mml-ieqn-34"><mml:mi mathvariant="normal">&#x03A9;</mml:mi></mml:math></inline-formula></term>
<def>
<p>Concentration difference parameter</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-35"><mml:math id="mml-ieqn-35"><mml:msub><mml:mi>h</mml:mi><mml:mn>3</mml:mn></mml:msub></mml:math></inline-formula></term>
<def>
<p>Microorganisms transfer coefficients</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-36"><mml:math id="mml-ieqn-36"><mml:mi>L</mml:mi><mml:mi>b</mml:mi></mml:math></inline-formula></term>
<def>
<p>Lewis number</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-37"><mml:math id="mml-ieqn-37"><mml:mi>P</mml:mi><mml:mi>e</mml:mi></mml:math></inline-formula></term>
<def>
<p>Peclet number</p>
</def>
</def-item>
</def-list>
</glossary>
<ack>
<p>The authors extend their sincere gratitude to the reviewers for their helpful suggestions, which significantly enhanced the quality and presentation of this paper.</p>
</ack>
<sec><title>Funding Statement</title>
<p>The authors received no specific funding for this study.</p>
</sec>
<sec><title>Author Contributions</title>
<p>Conceptualization, M.A.U.R. (Muhammad Abaid Ur Rehman) and M.A.F. (Muhammad Asif Farooq); methodology, M.A.U.R.; software, M.A.U.R.; validation, M.A.U.R. and M.A.F.; formal analysis, M.A.U.R. and A.H.M. (Ahmed M Hassan); investigation, M.A.U.R. and M.A.F.; resources, A.H.M., M.A.F.; data curation, M.A.U.R.; writing original draft preparation, M.A.U.R.; writing review and editing, M.A.U.R. and A.H.M.; visualization, M.A.U.R., A.H.M. and M.A.F.; supervision, M.A.F.; funding acquisition, A.H.M. All authors have read and agreed to the published version of the manuscript.</p>
</sec>
<sec sec-type="data-availability"><title>Availability of Data and Materials</title>
<p>The data generated in this study can be made available by corresponding author following a request.</p>
</sec>
<sec sec-type="COI-statement"><title>Conflicts of Interest</title>
<p>The authors declare that they have no conflicts of interest to report regarding the present study.</p>
</sec>
<ref-list content-type="authoryear">
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