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<front>
<journal-meta>
<journal-id journal-id-type="pmc">CMES</journal-id>
<journal-id journal-id-type="nlm-ta">CMES</journal-id>
<journal-id journal-id-type="publisher-id">CMES</journal-id>
<journal-title-group>
<journal-title>Computer Modeling in Engineering &#x0026; Sciences</journal-title>
</journal-title-group>
<issn pub-type="epub">1526-1506</issn>
<issn pub-type="ppub">1526-1492</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">74680</article-id>
<article-id pub-id-type="doi">10.32604/cmes.2025.074680</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Article</subject>
</subj-group>
</article-categories>
<title-group>
<article-title>Gradient Descent-Based Prediction of Heat-Transmission Rate of Engine Oil-Based Hybrid Nanofluid over Trapezoidal and Rectangular Fins for Sustainable Energy Systems</article-title>
<alt-title alt-title-type="left-running-head">Gradient Descent-Based Prediction of Heat-Transmission Rate of Engine Oil-Based Hybrid Nanofluid over Trapezoidal and Rectangular Fins for Sustainable Energy Systems</alt-title>
<alt-title alt-title-type="right-running-head">Gradient Descent-Based Prediction of Heat-Transmission Rate of Engine Oil-Based Hybrid Nanofluid over Trapezoidal and Rectangular Fins for Sustainable Energy Systems</alt-title>
</title-group>
<contrib-group>
<contrib id="author-1" contrib-type="author">
<name name-style="western"><surname>Kumar</surname><given-names>Maddina Dinesh</given-names></name><xref ref-type="aff" rid="aff-1">1</xref><xref ref-type="author-notes" rid="afn1">#</xref></contrib>
<contrib id="author-2" contrib-type="author">
<name name-style="western"><surname>Mamatha</surname><given-names>S. U.</given-names></name><xref ref-type="aff" rid="aff-2">2</xref></contrib>
<contrib id="author-3" contrib-type="author">
<name name-style="western"><surname>Masood</surname><given-names>Khalid</given-names></name><xref ref-type="aff" rid="aff-3">3</xref></contrib>
<contrib id="author-4" contrib-type="author">
<name name-style="western"><surname>Shah</surname><given-names>Nehad Ali</given-names></name><xref ref-type="aff" rid="aff-4">4</xref><xref ref-type="author-notes" rid="afn1">#</xref></contrib>
<contrib id="author-5" contrib-type="author" corresp="yes">
<name name-style="western"><surname>Yook</surname><given-names>Se-Jin</given-names></name><xref ref-type="aff" rid="aff-1">1</xref><email>ysjnuri@hanyang.ac.kr</email></contrib>
<aff id="aff-1"><label>1</label><institution>School of Mechanical Engineering, Hanyang University, 222 Wangsimni-ro, Seongdong-gu</institution>, <addr-line>Seoul, 04763</addr-line>, <country>Republic of Korea</country></aff>
<aff id="aff-2"><label>2</label><institution>Faculty of Mathematics, Institute of Management, Kristu Jayanti Deemed to be University, K. Narayanapura</institution>, <addr-line>Kothanur, Bengaluru, 560077</addr-line>, <country>India</country></aff>
<aff id="aff-3"><label>3</label><institution>Department of Mathematics and Statistics, College of Science, Imam Mohammad Ibn Saud Islamic University (IMSIU)</institution>, <addr-line>Riyadh, 11623</addr-line>, <country>Saudi Arabia</country></aff>
<aff id="aff-4"><label>4</label><institution>Department of Mechanical Engineering, Sejong University</institution>, <addr-line>Seoul, 05006</addr-line>, <country>Republic of Korea</country></aff>
</contrib-group>
<author-notes>
<corresp id="cor1"><label>&#x002A;</label>Corresponding Author: Se-Jin Yook. Email: <email>ysjnuri@hanyang.ac.kr</email></corresp>
<fn id="afn1">
<p><sup>#</sup>These authors contributed equally to this work</p>
</fn>
</author-notes>
<pub-date date-type="collection" publication-format="electronic">
<year>2026</year>
</pub-date>
<pub-date date-type="pub" publication-format="electronic">
<day>29</day><month>1</month><year>2026</year>
</pub-date>
<volume>146</volume>
<issue>1</issue>
<elocation-id>20</elocation-id>
<history>
<date date-type="received">
<day>15</day>
<month>10</month>
<year>2025</year>
</date>
<date date-type="accepted">
<day>28</day>
<month>11</month>
<year>2025</year>
</date>
</history>
<permissions>
<copyright-statement>&#x00A9; 2026 The Authors.</copyright-statement>
<copyright-year>2026</copyright-year>
<copyright-holder>Published by Tech Science Press.</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_CMES_74680.pdf"></self-uri>
<abstract>
<p>Fluid dynamic research on rectangular and trapezoidal fins is aimed at increasing heat transfer by means of large surfaces. The trapezoidal cavity form is compared with its thermal and flow performance, and it is revealed that trapezoidal fins tend to be more efficient, particularly when material optimization is critical. Motivated by the increasing need for sustainable energy management, this work analyses the thermal performance of inclined trapezoidal and rectangular porous fins utilising a unique hybrid nanofluid. The effectiveness of nanoparticles in a working fluid is primarily determined by their thermophysical properties; hence, optimising these properties can significantly improve overall performance. This study considers the dispersion of Graphene Oxide <inline-formula id="ieqn-1"><mml:math id="mml-ieqn-1"><mml:mrow><mml:mo>(</mml:mo><mml:mi>G</mml:mi><mml:mi>O</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> and Molybdenum Disulfide in the base fluid, engine oil. Temperature profiles are analysed by altering the radiative, porosity, wet porous, and angle of inclination parameters. Surface and contour plots are constructed by using the Lobatto IIIa Collocation Method with BVP5C solver in MATLAB and Gradient Descent Optimisation to predict the combined heat transfer rate. According to the study, fluid temperature consistently decreases when the angle of inclination, wet porous parameter, porosity parameter, and radiative parameter increase, suggesting significantly improved heat dissipation. The trapezoidal fin consistently exhibits a superior heat transfer mechanism than a rectangular fin. It is found that the trapezoidal fin transmits heat at a rate that is 0.05% higher than that of the rectangular fin. Validation of the present study is done through the comparison of previous studies. This research provides useful design insights for sophisticated engineering uses, including electrical cooling devices, heat exchangers, radiators, and solar heaters.</p>
</abstract>
<kwd-group kwd-group-type="author">
<kwd>Rectangular fin</kwd>
<kwd>hybrid nanofluid</kwd>
<kwd>trapezoidal fin</kwd>
<kwd>angle of inclination</kwd>
<kwd>gradient descent optimization</kwd>
<kwd>Lobatto IIIa collocation method</kwd>
</kwd-group>
<funding-group>
<award-group id="awg1">
<funding-source>Seoul Metropolitan Government</funding-source>
<award-id>2025-RISE-01-027-04</award-id>
</award-group>
</funding-group>
</article-meta>
</front>
<body>
<sec id="s1">
<label>1</label>
<title>Introduction</title>
<p>Fin is referred to as a thin, elongated, extended structure attached to a solid surface. Engineers realised in the early 20th century that heat dissipation through convection may be improved by expanding a solid surface&#x2019;s surface area. Fins are widely employed in automotive, electronics, aerospace, steel, metallurgy and renewable energy industries to enhance heat transfer. The choice of fin type, size, shape, and spacing depends on the specific heat transfer requirements of the system and the constraints of the application. Fins with the best designs are in more demand. Aziz and Fang [<xref ref-type="bibr" rid="ref-1">1</xref>] examined temperature distribution in longitudinal fin focusing on trapezoidal, rectangular, and concave profiles. Han and Peng [<xref ref-type="bibr" rid="ref-2">2</xref>] investigated thermal management in a moving fin considering a radiative and convective environment. Pavithra et al. [<xref ref-type="bibr" rid="ref-3">3</xref>] analysed the temperature distribution in the dovetail longitudinal fin considering radiation and hybrid nanofluid. Riasat et al. [<xref ref-type="bibr" rid="ref-4">4</xref>] examined the Darcy model of internal heat generation in a radial fin. Luo et al. [<xref ref-type="bibr" rid="ref-5">5</xref>] used a deep generative model to analyse thermal performance in a fin. Abd-Elmonem et al. [<xref ref-type="bibr" rid="ref-6">6</xref>] analysed the heat transport via a fin in a vertical pipe using a machine learning technique. Rehman et al. [<xref ref-type="bibr" rid="ref-7">7</xref>] using ANN predicted improving buoyancy results in convective heat transfer in a T-shaped fin. Arshad [<xref ref-type="bibr" rid="ref-8">8</xref>] reported that the addition of a tree-shaped fin reduced heat sink temperature by 8%. Sowmya et al. [<xref ref-type="bibr" rid="ref-9">9</xref>] investigated thermal distribution in a rectangular fin incorporating magnetic and radiation. Basha et al. [<xref ref-type="bibr" rid="ref-10">10</xref>] investigated entropy generation and heat transport in nanofluid flow across a square enclosure fitted with a fin and estimated the optimal transport using machine learning technology. The development of extended surface technology has led to the replacement of conventional solid fin structures with porous ones. Conventional uses for heat transmission in porous media include solar collectors, heat exchangers, and reactor cooling. Kiwan and Al-Nimr [<xref ref-type="bibr" rid="ref-11">11</xref>] were the ones who first suggested using porous fins by presenting the Darcy model. They took up a comparative study between porous and conventional fins and noticed that the porous fin shows better performance in heat transfer. Ahmad et al. [<xref ref-type="bibr" rid="ref-12">12</xref>] applied an ANN model to analyse the optimal thermal dispersion considering a porous triangular moving fin by including radiation, surface temperature, and Peclet number parameters. Hu et al. [<xref ref-type="bibr" rid="ref-13">13</xref>] addressed thermal characteristics using structured porous fins. The study reported that structured porous fins (SPFs) significantly enhanced phase change material (PCM) heat transfer and achieved a 62% decrease in melting time. Alotaibi et al. [<xref ref-type="bibr" rid="ref-14">14</xref>] applied ANN and the ISPH method to analyse the optimal heat transfer performance. Their study reported that 15% of the temperature was reduced due to the addition of a triangular porous fin. Nandy and Balasubramanian [<xref ref-type="bibr" rid="ref-15">15</xref>] observed that a porous wavy fin in a microchannel improved thermos-hydraulic performance due to the use of design C at Re of 300.</p>
<p>The angle of inclination has a significant impact on fin performance. In particular, in natural convection, it influences the boundary layer growth, flow structure and the heat transfer coefficient. While in forced convection, it impacts the flow distribution and associated pressure drop. He et al. [<xref ref-type="bibr" rid="ref-16">16</xref>] asserted that by improving the inclination angle, the average heat transfer and heat flux of a solid-perforated spiral fin rose by 15.5%. Li et al. [<xref ref-type="bibr" rid="ref-17">17</xref>] demonstrated that micro-finned wall position and inclination angle play a crucial role in vapour-liquid distribution, heat transfer and flow dynamics. Dhaoui et al. [<xref ref-type="bibr" rid="ref-18">18</xref>] revealed that optimising fin angle remarkably enhances heat transfer and overall effectiveness of solar stills. Komathi et al. [<xref ref-type="bibr" rid="ref-19">19</xref>] carried out an analysis of heat transfer in an inclined wetted moving fin and reported that fin temperature declined with increasing wet porous, radiation, inclination angle and convective parameter. Zhong et al. [<xref ref-type="bibr" rid="ref-20">20</xref>] took up a detailed investigation on heat transfer considering four different fins, namely curved, vertical, serpentine and inclined fins. They noticed that heat transfer efficiency was more effective for the curved fin, and the serpentine fin exhibited outstanding heat transfer. Chen et al. [<xref ref-type="bibr" rid="ref-21">21</xref>] from 20 to 180 W, the bending heat type&#x2019;s heat transfer is greatly improved by the observed small inclination angle. Choi and Eastman [<xref ref-type="bibr" rid="ref-22">22</xref>] first showed that the deferment of nanoparticles in a working fluid, like oil, ethylene glycol, and water, can greatly enhance their thermal properties and heat transfer performance. Owing to these advantages, nanofluids are increasingly used in heat transfer applications in commercial and engineering industries. In recent years, attention has shifted towards hybrid and ternary nanofluids. Bahiraei et al. [<xref ref-type="bibr" rid="ref-23">23</xref>] conducted an experimental study and described a hybrid nanofluid&#x2019;s thermal characteristics, which involves the amalgamation of two distinct nanoparticles in a base fluid. Research confirms that hybrid nanofluid outperforms mono nanofluid with enhanced rheological characteristics. Ternary hybrid extends this concept by incorporating three distinct nanoparticles. Varatharaj et al. [<xref ref-type="bibr" rid="ref-24">24</xref>] analysed the impact of first-order slip, porous media, ternary hybrid nanofluid flow across a permeable stretching surface via joule heating and viscous dissipation. Mishra et al. [<xref ref-type="bibr" rid="ref-25">25</xref>] examined how slip affected a ternary hybrid nanofluid passing across a permeable plate. Gul et al. [<xref ref-type="bibr" rid="ref-26">26</xref>] elucidated that the incorporation of <inline-formula id="ieqn-2"><mml:math id="mml-ieqn-2"><mml:mi>A</mml:mi><mml:mi>u</mml:mi><mml:mo>,</mml:mo><mml:mi>F</mml:mi><mml:msub><mml:mi>e</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:msub><mml:mi>O</mml:mi><mml:mrow><mml:mn>3</mml:mn></mml:mrow></mml:msub><mml:mo>,</mml:mo><mml:mi>S</mml:mi><mml:mi>W</mml:mi><mml:mi>C</mml:mi><mml:mi>N</mml:mi><mml:mi>T</mml:mi></mml:math></inline-formula> Nanoparticles in Casson fluid enhances heat transfer. Anjum et al. [<xref ref-type="bibr" rid="ref-27">27</xref>] analysed Casson ternary hybrid nanofluid enhanced thermal performance in drug delivery. Hussain [<xref ref-type="bibr" rid="ref-28">28</xref>] investigated ternary hybrid nanofluid flow in biomedical applications. Jahan and Nasrin [<xref ref-type="bibr" rid="ref-29">29</xref>] found that the highest heat transfer in a microchannel heat exchanger was produced by combining graphene, boron nitride, and carbon nanotubes in a ratio of 4/3:1/3:1/3. Hemmat et al. [<xref ref-type="bibr" rid="ref-30">30</xref>] investigated experimentally how a ternary hybrid nanofluid can improve heat transfer.</p>
<p>A computational investigation of Cattaneo-Christov double diffusion and mixed convection effects in a non-Darcian Sutterby nanofluid was conducted by Rehman et al. [<xref ref-type="bibr" rid="ref-31">31</xref>] employing multi-objective optimization through Response Surface Methodology (RSM). Using a modified Buongiorno&#x2019;s model, Wang et al. [<xref ref-type="bibr" rid="ref-32">32</xref>] examined the heat and mass transport of an Ag&#x2013;H<sub>2</sub>O nano-thin film flowing over a porous medium. Rehman et al. [<xref ref-type="bibr" rid="ref-33">33</xref>] used response surface methods to study the impact of heat radiation and magnetohydrodynamics on shear-thinning Williamson nanofluids with stability analysis. Oscillatory convective gear-generalised differential quadrature analysis was studied by Xia et al. [<xref ref-type="bibr" rid="ref-34">34</xref>], Darcy-Forchheimer and Lorentz quadratic drag forces in second-grade fluids&#x2019; Taylor-Couette flows.</p>
<p><bold>Novelty of the Present Study:</bold></p>
<p>Despite extensive research on fin problems, inclined rectangular and triangular porous fins wetted with hybrid nanofluid remain largely unexplored with this combination. Therefore, because applications for sustainable energy systems are in high demand, this study aims to address the thermal performance of inclined porous rectangular and triangular porous fins wetted with a hybrid nanofluid (Engine Oil &#x002B; Graphene Oxide (GO) &#x002B; Molybdenum Disulfide (MOS<sub>2</sub>)) through machine learning gradient descent optimization technique forecasting the rate of heat transfer in rectangular and trapezoidal fins, the difference between expected and actual values is negligible, shows the precise thermal performance estimation for various fin geometries.</p>
</sec>
<sec id="s2">
<label>2</label>
<title>Mathematical Formulation</title>
<p>The interplay of conduction, convection, and radiation is used to analyse heat transmission in a fin. A differential control volume technique is used to move heat internally along the <italic>x</italic>-direction. The temperature gradient from the base temperature (<italic>T</italic><sub><italic>b</italic></sub>) causes the heat flux (<italic>qx</italic>) to change. Heat is lost through convection and radiation as it enters the surrounding environment after passing through the fin. The geometrical characteristics of the fin, including its thickness (<italic>tb</italic>), width (<italic>w</italic>), and length (<italic>L</italic>), are important in determining how heat is transferred and distributed. As internal conduction counteracts the heat loss at the surface, the temperature drops along the <italic>x</italic>-direction. Whereas radiative heat loss happens through thermal radiation to the surrounding environment at temperature (<italic>Ta</italic>), convective heat loss transfers energy to the surrounding fluid. The fin&#x2019;s ensuing temperature gradient shows how internal heat conduction and outward heat dissipation are balanced. Comprehending these principles is essential for maximising thermal management in engineering systems, guaranteeing efficient heat dissipation for enhanced stability and performance.</p>
<p>The governing differential equation for this issue is provided by Khan et al. [<xref ref-type="bibr" rid="ref-35">35</xref>]
<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:mtd><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mi>d</mml:mi><mml:mrow><mml:mi>d</mml:mi><mml:mi>x</mml:mi></mml:mrow></mml:mfrac></mml:mstyle><mml:mrow><mml:mo>[</mml:mo><mml:msup><mml:mi>t</mml:mi><mml:mrow><mml:mo>&#x2217;</mml:mo></mml:mrow></mml:msup><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mi>d</mml:mi><mml:mi>T</mml:mi></mml:mrow><mml:mrow><mml:mi>d</mml:mi><mml:mi>x</mml:mi></mml:mrow></mml:mfrac></mml:mstyle><mml:mo>]</mml:mo></mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mstyle displaystyle="true" 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displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mn>2</mml:mn><mml:mi>&#x03C3;</mml:mi><mml:mi>&#x03B5;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:msup><mml:mi>T</mml:mi><mml:mrow><mml:mn>4</mml:mn></mml:mrow></mml:msup><mml:mo>&#x2212;</mml:mo><mml:msubsup><mml:mi>T</mml:mi><mml:mrow><mml:mi>a</mml:mi></mml:mrow><mml:mrow><mml:mn>4</mml:mn></mml:mrow></mml:msubsup><mml:mo>)</mml:mo></mml:mrow></mml:mrow><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:mo>&#x2212;</mml:mo><mml:mo>&#x2026;</mml:mo></mml:mtd></mml:mtr><mml:mtr><mml:mtd /><mml:mtd><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mn>2</mml:mn><mml:msub><mml:mi>h</mml:mi><mml:mrow><mml:mi>a</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>i</mml:mi><mml:mrow><mml:mi>f</mml:mi><mml:mi>g</mml:mi></mml:mrow></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mn>1</mml:mn><mml:mo>&#x2212;</mml:mo><mml:mi>&#x03D5;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C9;</mml:mi><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>&#x03C9;</mml:mi><mml:mrow><mml:mi>a</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow><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>a</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:mrow><mml:mrow><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>C</mml:mi><mml:mrow><mml:mi>p</mml:mi></mml:mrow></mml:msub><mml:mi>L</mml:mi><mml:msup><mml:mi>e</mml:mi><mml:mrow><mml:mfrac><mml:mn>2</mml:mn><mml:mn>3</mml:mn></mml:mfrac></mml:mrow></mml:msup><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi>b</mml:mi></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi>a</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:mrow></mml:mfrac></mml:mstyle><mml:mo>&#x2212;</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mn>2</mml:mn><mml:msub><mml:mi>h</mml:mi><mml:mrow><mml:mi>a</mml:mi></mml:mrow></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mn>1</mml:mn><mml:mo>&#x2212;</mml:mo><mml:mi>&#x03D5;</mml:mi><mml:mo>)</mml:mo></mml:mrow><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>a</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:mrow><mml:mrow><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</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>b</mml:mi></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi>a</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:mrow></mml:mfrac></mml:mstyle><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula>where, Hybrid nanofluid is denoted by the subscript <italic>hnf</italic>, <italic>C</italic> stands for specific heat capacity at constant pressure, &#x03D5; for porosity, &#x03B2; for thermal expansion coefficient, <italic>k</italic> for thermal diffusivity, &#x03BC; for effective kinematic viscosity, and &#x03C1; for effective mass density.</p>
<p>The following provides the corresponding boundary conditions:
<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:mtd><mml:mi>T</mml:mi><mml:mo>=</mml:mo><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi>b</mml:mi></mml:mrow></mml:msub><mml:mspace width="1em" /><mml:mi>a</mml:mi><mml:mi>t</mml:mi><mml:mspace width="1em" /><mml:mi>x</mml:mi><mml:mo>=</mml:mo><mml:mi>L</mml:mi></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula>
<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:mfrac><mml:mrow><mml:mi>d</mml:mi><mml:mi>T</mml:mi></mml:mrow><mml:mrow><mml:mi>d</mml:mi><mml:mi>x</mml:mi></mml:mrow></mml:mfrac><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mspace width="1em" /><mml:mi>a</mml:mi><mml:mi>t</mml:mi><mml:mspace width="1em" /><mml:mi>x</mml:mi><mml:mo>=</mml:mo><mml:mn>0.</mml:mn></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>The linearization of the <italic>T</italic><sup>4</sup> components as a function of temperature is possible with the Rosseland approximation, i.e., <inline-formula id="ieqn-3"><mml:math id="mml-ieqn-3"><mml:msup><mml:mi>T</mml:mi><mml:mrow><mml:mn>4</mml:mn></mml:mrow></mml:msup><mml:mo>=</mml:mo><mml:mn>4</mml:mn><mml:msubsup><mml:mi>T</mml:mi><mml:mrow><mml:mi>&#x03B1;</mml:mi></mml:mrow><mml:mrow><mml:mn>3</mml:mn></mml:mrow></mml:msubsup><mml:mi>T</mml:mi><mml:mo>&#x2212;</mml:mo><mml:mn>3</mml:mn><mml:msubsup><mml:mi>T</mml:mi><mml:mrow><mml:mi>&#x03B1;</mml:mi></mml:mrow><mml:mrow><mml:mn>4</mml:mn></mml:mrow></mml:msubsup></mml:math></inline-formula>.</p>
<p>Now consider the dimensionless quantities:
<disp-formula id="eqn-4"><label>(4)</label><mml:math id="mml-eqn-4" display="block"><mml:mi>X</mml:mi><mml:mo>=</mml:mo><mml:mfrac><mml:mi>x</mml:mi><mml:mi>L</mml:mi></mml:mfrac><mml:mo>,</mml:mo><mml:mi>&#x03B8;</mml:mi><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:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow></mml:msub></mml:mrow><mml:mrow><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi>b</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:mrow></mml:mfrac><mml:mo>.</mml:mo></mml:math></disp-formula></p>
<p><xref ref-type="disp-formula" rid="eqn-5">Eq. (5)</xref> is obtained after solving by substituting <xref ref-type="disp-formula" rid="eqn-4">Eq. (4)</xref> into <xref ref-type="disp-formula" rid="eqn-1">Eq. (1)</xref>
<disp-formula id="eqn-5"><label>(5)</label><mml:math id="mml-eqn-5" display="block"><mml:mtable columnalign="left" rowspacing="4pt" columnspacing="1em"><mml:mtr><mml:mtd><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:msup><mml:mi>d</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mi>&#x03B8;</mml:mi></mml:mrow><mml:mrow><mml:mi>d</mml:mi><mml:msup><mml:mi>X</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup></mml:mrow></mml:mfrac></mml:mstyle><mml:mo>&#x2212;</mml:mo><mml:mi>C</mml:mi><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mi>d</mml:mi><mml:mi>&#x03B8;</mml:mi></mml:mrow><mml:mrow><mml:mi>d</mml:mi><mml:mi>X</mml:mi></mml:mrow></mml:mfrac></mml:mstyle><mml:mo>&#x2212;</mml:mo><mml:mi>C</mml:mi><mml:mi>X</mml:mi><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:msup><mml:mi>d</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mi>&#x03B8;</mml:mi></mml:mrow><mml:mrow><mml:mi>d</mml:mi><mml:msup><mml:mi>X</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup></mml:mrow></mml:mfrac></mml:mstyle><mml:mo>&#x2212;</mml:mo><mml:mrow><mml:mo>(</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><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>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub><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:mstyle><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mo>(</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C1;</mml:mi><mml:mi>&#x03B2;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C1;</mml:mi><mml:mi>&#x03B2;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mo>(</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mi>&#x03BC;</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>&#x03BC;</mml:mi><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mo>(</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:mo>)</mml:mo></mml:mrow><mml:mi>S</mml:mi><mml:mi>h</mml:mi><mml:mi>sin</mml:mi><mml:mo>&#x2061;</mml:mo><mml:mi>&#x03C4;</mml:mi><mml:msup><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mo>&#x2212;</mml:mo><mml:mo>&#x2026;</mml:mo></mml:mtd></mml:mtr><mml:mtr><mml:mtd><mml:mi>N</mml:mi><mml:mi>r</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:mo>)</mml:mo></mml:mrow><mml:mi>&#x03B8;</mml:mi><mml:mo>&#x2212;</mml:mo><mml:mrow><mml:mo>(</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:mo>)</mml:mo></mml:mrow><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:msup><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>Following the non-depersonalization process, the boundary conditions turn into
<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>&#x03B8;</mml:mi><mml:mo>=</mml:mo><mml:mn>1</mml:mn><mml:mspace width="1em" /><mml:mi>a</mml:mi><mml:mi>t</mml:mi><mml:mspace width="1em" /><mml:mi>X</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula>
<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:mtd><mml:mfrac><mml:mrow><mml:mi>d</mml:mi><mml:mi>&#x03B8;</mml:mi></mml:mrow><mml:mrow><mml:mi>d</mml:mi><mml:mi>X</mml:mi></mml:mrow></mml:mfrac><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mspace width="1em" /><mml:mi>a</mml:mi><mml:mi>t</mml:mi><mml:mspace width="1em" /><mml:mi>X</mml:mi><mml:mo>=</mml:mo><mml:mn>1</mml:mn></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p>
<p>In the present study, normalization parameters are:</p>
<p><inline-formula id="ieqn-4"><mml:math id="mml-ieqn-4"><mml:mi>N</mml:mi><mml:mi>r</mml:mi><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mn>4</mml:mn><mml:mi>&#x03C3;</mml:mi><mml:mi>&#x03B5;</mml:mi><mml:msubsup><mml:mi>T</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x221E;</mml:mi></mml:mrow><mml:mrow><mml:mn>3</mml:mn></mml:mrow></mml:msubsup><mml:msup><mml:mi>L</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup></mml:mrow><mml:mrow><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:mi>t</mml:mi></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula> is the radiation parameter,</p>
<p><inline-formula id="ieqn-5"><mml:math id="mml-ieqn-5"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>0</mml:mn></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mn>2</mml:mn><mml:mi>h</mml:mi><mml:mi>a</mml:mi><mml:msup><mml:mi>L</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mrow><mml:mo>(</mml:mo><mml:mn>1</mml:mn><mml:mo>&#x2212;</mml:mo><mml:mi>&#x03D5;</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:mrow><mml:mrow><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>t</mml:mi><mml:mrow><mml:mi>b</mml:mi></mml:mrow></mml:msub></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula>, <inline-formula id="ieqn-6"><mml:math id="mml-ieqn-6"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>1</mml:mn></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mn>2</mml:mn><mml:mi>h</mml:mi><mml:mi>a</mml:mi><mml:msup><mml:mi>L</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mrow><mml:mo>(</mml:mo><mml:mn>1</mml:mn><mml:mo>&#x2212;</mml:mo><mml:mi>&#x03D5;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:msub><mml:mi>i</mml:mi><mml:mrow><mml:mi>f</mml:mi><mml:mi>g</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>b</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:mrow><mml:mrow><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>t</mml:mi><mml:mrow><mml:mi>b</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>C</mml:mi><mml:mrow><mml:mi>p</mml:mi></mml:mrow></mml:msub><mml:mi>L</mml:mi><mml:msup><mml:mi>e</mml:mi><mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mrow><mml:mn>3</mml:mn></mml:mrow></mml:mrow></mml:msup></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula>, <inline-formula id="ieqn-7"><mml:math id="mml-ieqn-7"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>0</mml:mn></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>1</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula> is the wet porosity parameter,</p>
<p><inline-formula id="ieqn-8"><mml:math id="mml-ieqn-8"><mml:mi>S</mml:mi><mml:mi>h</mml:mi><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mi>D</mml:mi><mml:mi>a</mml:mi><mml:mi>R</mml:mi><mml:mi>a</mml:mi></mml:mrow><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:msup><mml:mrow><mml:mo>(</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mi>L</mml:mi><mml:mi>t</mml:mi></mml:mfrac></mml:mstyle><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup></mml:math></inline-formula> Is the porosity parameter,</p>
<p><inline-formula id="ieqn-9"><mml:math id="mml-ieqn-9"><mml:mrow><mml:mo>(</mml:mo><mml:mi>x</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mo>=</mml:mo><mml:msub><mml:mi>t</mml:mi><mml:mrow><mml:mi>b</mml:mi></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:mi>&#x03B4;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mi>x</mml:mi><mml:mi>L</mml:mi></mml:mfrac></mml:mstyle><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> is the local semi-finish thickness,</p>
<p><inline-formula id="ieqn-10"><mml:math id="mml-ieqn-10"><mml:mi>&#x03C9;</mml:mi><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>&#x03C9;</mml:mi><mml:mrow><mml:mi>a</mml:mi></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:msub><mml:mi>b</mml:mi><mml:mrow><mml:mn>2</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>a</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula>.</p>
<p>For ease of simplification,</p>
<p>Let <inline-formula id="ieqn-11"><mml:math id="mml-ieqn-11"><mml:mi>a</mml:mi><mml:mo>=</mml:mo><mml:mi>N</mml:mi><mml:mi>r</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula></p>
<p><inline-formula id="ieqn-12"><mml:math id="mml-ieqn-12"><mml:mi>b</mml:mi><mml:mo>=</mml:mo><mml:mrow><mml:mo>(</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><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>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub><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:mstyle><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mo>(</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C1;</mml:mi><mml:mi>&#x03B2;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C1;</mml:mi><mml:mi>&#x03B2;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mo>(</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mi>&#x03BC;</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>&#x03BC;</mml:mi><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mo>(</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:mo>)</mml:mo></mml:mrow><mml:mi>S</mml:mi><mml:mi>h</mml:mi><mml:mi>sin</mml:mi><mml:mo>&#x2061;</mml:mo><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C4;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mo>+</mml:mo><mml:mrow><mml:mo>(</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:mo>)</mml:mo></mml:mrow><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula>.</p>
<p>Now the equation becomes,
<disp-formula id="eqn-8"><label>(8)</label><mml:math id="mml-eqn-8" display="block"><mml:mfrac><mml:mrow><mml:msup><mml:mi>d</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mi>&#x03B8;</mml:mi></mml:mrow><mml:mrow><mml:mi>d</mml:mi><mml:msup><mml:mi>X</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup></mml:mrow></mml:mfrac><mml:mo>&#x2212;</mml:mo><mml:mi>C</mml:mi><mml:mfrac><mml:mrow><mml:mi>d</mml:mi><mml:mi>&#x03B8;</mml:mi></mml:mrow><mml:mrow><mml:mi>d</mml:mi><mml:mi>X</mml:mi></mml:mrow></mml:mfrac><mml:mo>&#x2212;</mml:mo><mml:mi>C</mml:mi><mml:mi>X</mml:mi><mml:mfrac><mml:mrow><mml:msup><mml:mi>d</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mi>&#x03B8;</mml:mi></mml:mrow><mml:mrow><mml:mi>d</mml:mi><mml:msup><mml:mi>X</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup></mml:mrow></mml:mfrac><mml:mo>&#x2212;</mml:mo><mml:mi>b</mml:mi><mml:msup><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mo>&#x2212;</mml:mo><mml:mi>a</mml:mi><mml:mi>&#x03B8;</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:math></disp-formula></p>
<p>Fin&#x2019;s heat transfer rate by using the study of Khan et al. [<xref ref-type="bibr" rid="ref-35">35</xref>]:
<disp-formula id="ueqn-9"><mml:math id="mml-ueqn-9" display="block"><mml:mi>Q</mml:mi><mml:mo>=</mml:mo><mml:mo>&#x2212;</mml:mo><mml:mfrac><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac><mml:msup><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x2032;</mml:mi></mml:mrow></mml:msup><mml:mrow><mml:mo>(</mml:mo><mml:mn>0</mml:mn><mml:mo>)</mml:mo></mml:mrow></mml:math></disp-formula></p>
</sec>
<sec id="s3">
<label>3</label>
<title>Methodology of the Present Study</title>
<sec id="s3_1">
<label>3.1</label>
<title>Lobatto IIIa Collocation Method</title>
<p><list list-type="bullet">
<list-item>
<p>The given boundary conditions are then turned into a first-order system of differential equations, formulating the boundary value problem.
<disp-formula id="ueqn-11"><mml:math id="mml-ueqn-11" display="block"><mml:mtable columnalign="left left left" rowspacing="4pt" columnspacing="1em"><mml:mtr><mml:mtd><mml:mi>&#x03B8;</mml:mi><mml:mo>=</mml:mo><mml:msub><mml:mi>f</mml:mi><mml:mrow><mml:mn>1</mml:mn></mml:mrow></mml:msub><mml:mo>,</mml:mo><mml:msup><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mi mathvariant="normal">&#x2032;</mml:mi></mml:mrow></mml:msup><mml:mo>=</mml:mo><mml:msub><mml:mi>f</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:mtd></mml:mtr><mml:mtr><mml:mtd><mml:mi>B</mml:mi><mml:mi>o</mml:mi><mml:mi>u</mml:mi><mml:mi>n</mml:mi><mml:mi>d</mml:mi><mml:mi>a</mml:mi><mml:mi>r</mml:mi><mml:mi>y</mml:mi><mml:mspace width="thinmathspace" /><mml:mi>C</mml:mi><mml:mi>o</mml:mi><mml:mi>n</mml:mi><mml:mi>d</mml:mi><mml:mi>i</mml:mi><mml:mi>t</mml:mi><mml:mi>i</mml:mi><mml:mi>o</mml:mi><mml:mi>n</mml:mi><mml:mi>s</mml:mi></mml:mtd></mml:mtr><mml:mtr><mml:mtd><mml:msub><mml:mi>f</mml:mi><mml:mrow><mml:mi>a</mml:mi></mml:mrow></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mn>1</mml:mn><mml:mo>)</mml:mo></mml:mrow><mml:mo>=</mml:mo><mml:mn>1</mml:mn></mml:mtd></mml:mtr><mml:mtr><mml:mtd><mml:msub><mml:mi>f</mml:mi><mml:mrow><mml:mi>b</mml:mi></mml:mrow></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mn>2</mml:mn><mml:mo>)</mml:mo></mml:mrow><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p></list-item>
<list-item>
<p>The first mesh is created on the solution interval, and a good initial guess of the solution is provided.
<disp-formula id="ueqn-12"><mml:math id="mml-ueqn-12" display="block"><mml:mi>I</mml:mi><mml:mi>n</mml:mi><mml:mi>i</mml:mi><mml:mi>t</mml:mi><mml:mi>i</mml:mi><mml:mi>a</mml:mi><mml:mi>l</mml:mi><mml:mi>G</mml:mi><mml:mi>u</mml:mi><mml:mi>e</mml:mi><mml:mi>s</mml:mi><mml:mi>s</mml:mi><mml:mo>=</mml:mo><mml:mrow><mml:mo>{</mml:mo><mml:mn>0.1</mml:mn><mml:mo>,</mml:mo><mml:mn>0.1</mml:mn><mml:mo>}</mml:mo></mml:mrow></mml:math></disp-formula></p></list-item>
<list-item>
<p>The ordinary differential equation (ODE) system is expressed as a function, and the boundary conditions are expressed as a separate boundary condition function.</p></list-item>
<list-item>
<p>The Lobatto IIIa collocation approach is an internal approach used in the bvp5c solver of MATLAB to impose accuracy at collocation points.</p></list-item>
<list-item>
<p>Tolerance error is <bold>10</bold><sup><bold>&#x2212;3</bold></sup>, Step size is <bold>0.01</bold> and computational time is <bold>5 s</bold>.</p></list-item>
<list-item>
<p>The solver automatically optimises the mesh to meet error tolerances, and the solver is numerically stable.</p></list-item>
</list></p>
</sec>
<sec id="s3_2">
<label>3.2</label>
<title>Gradient Descent Machine Learning</title>
<p><list list-type="bullet">
<list-item>
<p><bold>Input:</bold> Observe and preprocess the input information of important physical parameters.</p></list-item>
<list-item>
<p><bold>Influence of Features:</bold> Research the effect of parameters on physical quantities of the target.</p></list-item>
<list-item>
<p><bold>Model Training:</bold> Finding a minimum loss of a machine learning algorithm using gradient descent. The Cost function is <inline-formula id="ieqn-13"><mml:math id="mml-ieqn-13"><mml:mi>J</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mn>0</mml:mn></mml:mrow></mml:msub><mml:mo>,</mml:mo><mml:msub><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mn>1</mml:mn></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mo>=</mml:mo><mml:mfrac><mml:mn>1</mml:mn><mml:mrow><mml:mn>2</mml:mn><mml:mi>n</mml:mi></mml:mrow></mml:mfrac><mml:munderover><mml:mo>&#x2211;</mml:mo><mml:mrow><mml:mi>i</mml:mi><mml:mo>=</mml:mo><mml:mn>1</mml:mn></mml:mrow><mml:mrow><mml:mi>n</mml:mi></mml:mrow></mml:munderover><mml:msup><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mn>0</mml:mn></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:msub><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mn>1</mml:mn></mml:mrow></mml:msub><mml:msub><mml:mi>x</mml:mi><mml:mrow><mml:mi>i</mml:mi></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mi>i</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mo>.</mml:mo></mml:math></inline-formula><disp-formula id="ueqn-112"><mml:math id="mml-ueqn-112" display="block"><mml:mtable columnalign="left" rowspacing="4pt" columnspacing="1em"><mml:mtr><mml:mtd><mml:mi>J</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mn>0</mml:mn></mml:mrow></mml:msub><mml:mo>,</mml:mo><mml:msub><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mn>1</mml:mn></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mo>=</mml:mo><mml:mrow><mml:mtext>Cos</mml:mtext></mml:mrow><mml:mspace width="thinmathspace" /><mml:mi>t</mml:mi><mml:mspace width="thinmathspace" 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/><mml:mrow><mml:mtext>&#xA0;Output</mml:mtext></mml:mrow></mml:mtd></mml:mtr><mml:mtr><mml:mtd><mml:msub><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mn>0</mml:mn></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:msub><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mn>1</mml:mn></mml:mrow></mml:msub><mml:msub><mml:mi>x</mml:mi><mml:mrow><mml:mi>i</mml:mi></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mi>i</mml:mi></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:mi>R</mml:mi><mml:mi>e</mml:mi><mml:mi>s</mml:mi><mml:mi>i</mml:mi><mml:mi>d</mml:mi><mml:mi>u</mml:mi><mml:mi>e</mml:mi><mml:mspace width="thinmathspace" /><mml:mi>E</mml:mi><mml:mi>r</mml:mi><mml:mi>r</mml:mi><mml:mi>o</mml:mi><mml:mi>r</mml:mi><mml:mo>,</mml:mo><mml:msup><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mn>0</mml:mn></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:msub><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mn>1</mml:mn></mml:mrow></mml:msub><mml:msub><mml:mi>x</mml:mi><mml:mrow><mml:mi>i</mml:mi></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>y</mml:mi><mml:mrow><mml:mi>i</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mo>=</mml:mo><mml:mi>S</mml:mi><mml:mi>q</mml:mi><mml:mi>u</mml:mi><mml:mi>a</mml:mi><mml:mi>r</mml:mi><mml:mi>e</mml:mi><mml:mspace width="thinmathspace" /><mml:mi>E</mml:mi><mml:mi>r</mml:mi><mml:mi>r</mml:mi><mml:mi>o</mml:mi><mml:mi>r</mml:mi></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula></p></list-item>
<list-item>
<p><bold>Analysis:</bold> Producing the predictions of linear fits and determining their performance using such measures as mean squared error (MSE) and root mean squared error (RMSE).</p></list-item>
</list></p>
</sec>
</sec>
<sec id="s4">
<label>4</label>
<title>Results and Discussion</title>
<p>An inclined longitudinal porous fin wetted with a hybrid nanofluid (Engine Oil Graphene Oxide Molybdenum Disulfide <inline-formula id="ieqn-14"><mml:math id="mml-ieqn-14"><mml:mrow><mml:mo>(</mml:mo><mml:mi>M</mml:mi><mml:mi>O</mml:mi><mml:msub><mml:mi>S</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula>) is studied numerically for both rectangular and trapezoidal fins. Temperature profiles <inline-formula id="ieqn-15"><mml:math id="mml-ieqn-15"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> is analysed for rectangular and trapezoidal fins by altering the radiative parameter, porosity parameter, wet porous parameter, and angle of inclination. The thermophysical property relations are shown in <xref ref-type="table" rid="table-1">Table 1</xref>, the thermophysical properties of the base fluid engine oil and the nanoparticles are listed in <xref ref-type="table" rid="table-2">Table 2</xref> and <xref ref-type="table" rid="table-3">Table 3</xref> displays the change in heat transfer rate of the porous rectangular and trapezoidal wet fin with hybrid nanofluid as determined by the numerical model and Gradient Descent algorithm for various scales of governing parameters (<inline-formula id="ieqn-16"><mml:math id="mml-ieqn-16"><mml:mi>T</mml:mi><mml:mo>,</mml:mo><mml:mi>S</mml:mi><mml:mi>h</mml:mi><mml:mo>,</mml:mo><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula> and <inline-formula id="ieqn-17"><mml:math id="mml-ieqn-17"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula>). Heat transfer rate shows a substantial enhancement with an increase in the degree of inclination <inline-formula id="ieqn-18"><mml:math id="mml-ieqn-18"><mml:mrow><mml:mo>(</mml:mo><mml:mi>T</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula>, parameter for wet porous <inline-formula id="ieqn-19"><mml:math id="mml-ieqn-19"><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula>, porosity parameter <inline-formula id="ieqn-20"><mml:math id="mml-ieqn-20"><mml:mrow><mml:mo>(</mml:mo><mml:mi>S</mml:mi><mml:mi>h</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> and radiative parameter <inline-formula id="ieqn-21"><mml:math id="mml-ieqn-21"><mml:mrow><mml:mo>(</mml:mo><mml:mi>N</mml:mi><mml:mi>r</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> for both rectangular and trapezoidal fins. Among the two geometries, the trapezoidal fin exhibits superior heat transfer performance compared to the rectangular fin, making it an ideal choice for advanced thermal management applications. From the obtained values, it is evident that the observed variations between both the approaches, gradient descent and numerical, are very minimal, typically below 1%&#x2013;1.5%, confirming the reliability and accuracy of the Optimization technique. These observations confirm the accuracy, reliability, and physical consistency of the proposed model in forecasting the trapezoidal and rectangular porous fins&#x2019; thermal response. The accuracy and dependability of the current study are demonstrated by <xref ref-type="table" rid="table-4">Table 4</xref>, which compares, under specific conditions, the findings of the current investigation with those of the previous study. <xref ref-type="fig" rid="fig-1">Fig. 1</xref> shows the applications of the current research, <xref ref-type="fig" rid="fig-2">Fig. 2</xref> shows a schematic representation of the trapezoidal and rectangular fin, <xref ref-type="fig" rid="fig-3">Fig. 3</xref> shows how the Gradient Descent Algorithm works, and <xref ref-type="fig" rid="fig-4">Fig. 4</xref> shows the methodology used in this study.</p>
<table-wrap id="table-1">
<label>Table 1</label>
<caption>
<title>Thermophysical property relations from the study Abbas and Mahmood [<xref ref-type="bibr" rid="ref-36">36</xref>]</title>
</caption>
<table>
<colgroup>
<col align="center"/>
<col align="left"/> </colgroup>
<thead>
<tr>
<th>Properties</th>
<th align="center">Hybrid nanofluid</th>
</tr>
</thead>
<tbody>
<tr>
<td>Viscosity</td>
<td><inline-formula id="ieqn-22"><mml:math id="mml-ieqn-22"><mml:msub><mml:mi>&#x03BC;</mml:mi><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mi>&#x03BC;</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:mrow><mml:msup><mml:mrow><mml:mo>(</mml:mo><mml:mn>1</mml:mn><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mi>G</mml:mi><mml:mi>O</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mn>2.5</mml:mn></mml:mrow></mml:msup><mml:msup><mml:mrow><mml:mo>(</mml:mo><mml:mn>1</mml:mn><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mi>M</mml:mi><mml:mi>O</mml:mi><mml:mrow><mml:msub><mml:mi>S</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mn>2.5</mml:mn></mml:mrow></mml:msup></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula></td>
</tr>
<tr>
<td>Density</td>
<td><inline-formula id="ieqn-23"><mml:math id="mml-ieqn-23"><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mi>&#x03C1;</mml:mi><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>&#x03C1;</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:mo>=</mml:mo><mml:mrow><mml:mo>(</mml:mo><mml:mn>1</mml:mn><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mi>G</mml:mi><mml:mi>O</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mo>[</mml:mo><mml:mrow><mml:mo>(</mml:mo><mml:mn>1</mml:mn><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mi>M</mml:mi><mml:mi>O</mml:mi><mml:mrow><mml:msub><mml:mi>S</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mo>+</mml:mo><mml:msub><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mi>M</mml:mi><mml:mi>O</mml:mi><mml:mrow><mml:msub><mml:mi>S</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:mrow></mml:msub><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mi>&#x03C1;</mml:mi><mml:mrow><mml:mi>M</mml:mi><mml:mi>O</mml:mi><mml:mrow><mml:msub><mml:mi>S</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:mrow></mml:msub><mml:msub><mml:mi>&#x03C1;</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:mo>]</mml:mo></mml:mrow><mml:mo>+</mml:mo><mml:msub><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mi>G</mml:mi><mml:mi>O</mml:mi></mml:mrow></mml:msub><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mi>&#x03C1;</mml:mi><mml:mrow><mml:mi>G</mml:mi><mml:mi>O</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>&#x03C1;</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle></mml:math></inline-formula></td>
</tr>
<tr>
<td>Heat capacity</td>
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</tr>
<tr>
<td>Thermal conductivity</td>
<td><inline-formula id="ieqn-25"><mml:math id="mml-ieqn-25"><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>G</mml:mi><mml:mi>O</mml:mi></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:mn>2</mml:mn><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:mn>2</mml:mn><mml:msub><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mi>G</mml:mi><mml:mi>O</mml:mi></mml:mrow></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>G</mml:mi><mml:mi>O</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:mrow><mml:mrow><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>G</mml:mi><mml:mi>O</mml:mi></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:mn>2</mml:mn><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:msub><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mi>G</mml:mi><mml:mi>O</mml:mi></mml:mrow></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>G</mml:mi><mml:mi>O</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:mrow></mml:mfrac></mml:mstyle><mml:mo>;</mml:mo></mml:math></inline-formula><inline-formula id="ieqn-26"><mml:math id="mml-ieqn-26"><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:mo>=</mml:mo><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>M</mml:mi><mml:mi>O</mml:mi><mml:mrow><mml:msub><mml:mi>S</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:mn>2</mml:mn><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:mn>2</mml:mn><mml:msub><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mi>M</mml:mi><mml:mi>O</mml:mi><mml:mrow><mml:msub><mml:mi>S</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:mrow></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>M</mml:mi><mml:mi>O</mml:mi><mml:mrow><mml:msub><mml:mi>S</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:mrow><mml:mrow><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>M</mml:mi><mml:mi>O</mml:mi><mml:mrow><mml:msub><mml:mi>S</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:mn>2</mml:mn><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:mo>+</mml:mo><mml:mn>2</mml:mn><mml:msub><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mi>M</mml:mi><mml:mi>O</mml:mi><mml:mrow><mml:msub><mml:mi>S</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:mrow></mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>k</mml:mi><mml:mrow><mml:mi>M</mml:mi><mml:mi>O</mml:mi><mml:mrow><mml:msub><mml:mi>S</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula></td>
</tr>
<tr>
<td>Thermal expansion</td>
<td><inline-formula id="ieqn-27"><mml:math id="mml-ieqn-27"><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C1;</mml:mi><mml:mi>&#x03B2;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C1;</mml:mi><mml:mi>&#x03B2;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:mo>=</mml:mo><mml:mrow><mml:mo>(</mml:mo><mml:mn>1</mml:mn><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mi>G</mml:mi><mml:mi>O</mml:mi></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mo>[</mml:mo><mml:mrow><mml:mo>(</mml:mo><mml:mn>1</mml:mn><mml:mo>&#x2212;</mml:mo><mml:msub><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mi>M</mml:mi><mml:mi>O</mml:mi><mml:mrow><mml:msub><mml:mi>S</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow><mml:mo>+</mml:mo><mml:msub><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mi>M</mml:mi><mml:mi>O</mml:mi><mml:mrow><mml:msub><mml:mi>S</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:mrow></mml:msub><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C1;</mml:mi><mml:mi>&#x03B2;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mi>M</mml:mi><mml:mi>O</mml:mi><mml:mrow><mml:msub><mml:mi>S</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:mrow></mml:msub><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C1;</mml:mi><mml:mi>&#x03B2;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle><mml:mo>]</mml:mo></mml:mrow><mml:mo>+</mml:mo><mml:msub><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mi>G</mml:mi><mml:mi>O</mml:mi></mml:mrow></mml:msub><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C1;</mml:mi><mml:mi>&#x03B2;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mi>G</mml:mi><mml:mi>O</mml:mi></mml:mrow></mml:msub><mml:msub><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C1;</mml:mi><mml:mi>&#x03B2;</mml:mi><mml:mo>)</mml:mo></mml:mrow><mml:mrow><mml:mi>f</mml:mi></mml:mrow></mml:msub></mml:mfrac></mml:mstyle></mml:math></inline-formula></td>
</tr>
</tbody>
</table>
</table-wrap><table-wrap id="table-2">
<label>Table 2</label>
<caption>
<title>Thermophysical properties</title>
</caption>
<table>
<colgroup>
<col align="center"/>
<col align="center"/>
<col align="center"/>
<col align="center"/>
<col align="center"/>
<col align="center"/> </colgroup>
<thead>
<tr>
<th></th>
<th>Nomenclature of nano-particles and base fluid</th>
<th><inline-formula id="ieqn-28"><mml:math id="mml-ieqn-28"><mml:mi>&#x03C1;</mml:mi></mml:math></inline-formula> <inline-formula id="ieqn-29"><mml:math id="mml-ieqn-29"><mml:mrow><mml:mo>(</mml:mo><mml:mrow><mml:mtext>kg</mml:mtext></mml:mrow><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:msup><mml:mrow><mml:mtext>m</mml:mtext></mml:mrow><mml:mrow><mml:mn>3</mml:mn></mml:mrow></mml:msup><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-30"><mml:math id="mml-ieqn-30"><mml:msub><mml:mi>C</mml:mi><mml:mrow><mml:mi>p</mml:mi></mml:mrow></mml:msub></mml:math></inline-formula> <inline-formula id="ieqn-31"><mml:math id="mml-ieqn-31"><mml:mrow><mml:mo>(</mml:mo><mml:mrow><mml:mtext>J</mml:mtext></mml:mrow><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mrow><mml:mtext>kgK</mml:mtext></mml:mrow><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-32"><mml:math id="mml-ieqn-32"><mml:mi>K</mml:mi></mml:math></inline-formula> <inline-formula id="ieqn-33"><mml:math id="mml-ieqn-33"><mml:mrow><mml:mo>(</mml:mo><mml:mrow><mml:mtext>W</mml:mtext></mml:mrow><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mrow><mml:mtext>mK</mml:mtext></mml:mrow><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula></th>
<th><inline-formula id="ieqn-34"><mml:math id="mml-ieqn-34"><mml:mi>&#x03B2;</mml:mi><mml:mo>&#x2217;</mml:mo><mml:msup><mml:mn>10</mml:mn><mml:mrow><mml:mo>&#x2212;</mml:mo><mml:mn>5</mml:mn></mml:mrow></mml:msup></mml:math></inline-formula><inline-formula id="ieqn-35"><mml:math id="mml-ieqn-35"><mml:mrow><mml:mo>(</mml:mo><mml:mn>1</mml:mn><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mrow><mml:mtext>K</mml:mtext></mml:mrow><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula></th>
</tr>
</thead>
<tbody>
<tr>
<td>Base fluid</td>
<td><inline-formula id="ieqn-36"><mml:math id="mml-ieqn-36"><mml:mi>E</mml:mi><mml:mi>n</mml:mi><mml:mi>g</mml:mi><mml:mi>i</mml:mi><mml:mi>n</mml:mi><mml:mi>e</mml:mi><mml:mi>O</mml:mi><mml:mi>i</mml:mi><mml:mi>l</mml:mi></mml:math></inline-formula></td>
<td>884</td>
<td>1910</td>
<td>0.144</td>
<td>70</td>
</tr>
<tr>
<td>Nanoparticles</td>
<td><inline-formula id="ieqn-37"><mml:math id="mml-ieqn-37"><mml:mi>G</mml:mi><mml:mi>r</mml:mi><mml:mi>a</mml:mi><mml:mi>p</mml:mi><mml:mi>h</mml:mi><mml:mi>e</mml:mi><mml:mi>n</mml:mi><mml:mi>e</mml:mi><mml:mi>O</mml:mi><mml:mi>x</mml:mi><mml:mi>i</mml:mi><mml:mi>d</mml:mi><mml:mi>e</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>G</mml:mi><mml:mi>O</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula></td>
<td>1800</td>
<td>717</td>
<td>5000</td>
<td>0.284</td>
</tr>
<tr>
<td></td>
<td><inline-formula id="ieqn-38"><mml:math id="mml-ieqn-38"><mml:mi>M</mml:mi><mml:mi>O</mml:mi><mml:msub><mml:mi>S</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula></td>
<td>5060</td>
<td>397.21</td>
<td>904.4</td>
<td>2.8424</td>
</tr>
<tr>
<td><inline-formula id="ieqn-39"><mml:math id="mml-ieqn-39"><mml:mtable columnalign="left" rowspacing="4pt" columnspacing="1em"><mml:mtr><mml:mtd><mml:mrow><mml:mtext>Rectangular Fin Case&#xA0;</mml:mtext></mml:mrow><mml:mrow><mml:mo>(</mml:mo><mml:mi>C</mml:mi><mml:mo>=</mml:mo><mml:mn>0</mml:mn><mml:mo>)</mml:mo></mml:mrow></mml:mtd></mml:mtr><mml:mtr><mml:mtd><mml:mrow><mml:mtext>Trapezoidal Fin Case&#xA0;</mml:mtext></mml:mrow><mml:mrow><mml:mo>(</mml:mo><mml:mi>C</mml:mi><mml:mo>&#x2260;</mml:mo><mml:mn>0</mml:mn><mml:mo>,</mml:mo><mml:mtext>&#x00A0;</mml:mtext><mml:mrow><mml:mtext>i.e.</mml:mtext></mml:mrow><mml:mo>,</mml:mo><mml:mrow><mml:mo>(</mml:mo><mml:mi>C</mml:mi><mml:mo>&#x227B;</mml:mo><mml:mn>0</mml:mn><mml:mo>)</mml:mo></mml:mrow><mml:mo>)</mml:mo></mml:mrow></mml:mtd></mml:mtr></mml:mtable></mml:math></inline-formula></td>
<td/>
<td/>
<td/>
<td/>
<td/>
</tr>
</tbody>
</table>
</table-wrap><table-wrap id="table-3">
<label>Table 3</label>
<caption>
<title>Heat transfer rate comparison of gradient descent and numerical results</title>
</caption>
<table>
<colgroup>
<col align="center"/>
<col align="center"/>
<col align="center"/>
<col align="center"/>
<col align="center"/>
<col align="center"/>
<col align="center"/>
<col align="center"/>
<col align="center"/>
<col align="center"/> </colgroup>
<thead>
<tr>
<th rowspan="2"><inline-formula id="ieqn-40"><mml:math id="mml-ieqn-40"><mml:mi>T</mml:mi></mml:math></inline-formula></th>
<th rowspan="2"><inline-formula id="ieqn-41"><mml:math id="mml-ieqn-41"><mml:mi>S</mml:mi><mml:mi>h</mml:mi></mml:math></inline-formula></th>
<th rowspan="2"><inline-formula id="ieqn-42"><mml:math id="mml-ieqn-42"><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula></th>
<th rowspan="2"><inline-formula id="ieqn-43"><mml:math id="mml-ieqn-43"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula></th>
<th colspan="2">Heat transfer rate numerical results</th>
<th colspan="2">Heat transfer rate gradient descent results</th>
<th colspan="2">Error in gradient descent</th>
</tr>
<tr>

<th align="center">Rectangular fin case</th>
<th align="center">Trapezoidal fin case</th>
<th align="center">Rectangular fin case</th>
<th align="center">Trapezoidal fin case</th>
<th align="center">Rectangular fin case</th>
<th align="center">Trapezoidal fin case</th>
</tr>
</thead>
<tbody>
<tr>
<td><inline-formula id="ieqn-44"><mml:math id="mml-ieqn-44"><mml:mi>&#x03C0;</mml:mi><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mn>6</mml:mn></mml:math></inline-formula></td>
<td></td>
<td></td>
<td></td>
<td>0.477685</td>
<td>0.497704</td>
<td>0.477935</td>
<td>0.497962</td>
<td>&#x2212;0.00025</td>
<td>&#x2212;0.000258</td>
</tr>
<tr>
<td><inline-formula id="ieqn-45"><mml:math id="mml-ieqn-45"><mml:mi>&#x03C0;</mml:mi><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mn>4</mml:mn></mml:math></inline-formula></td>
<td></td>
<td></td>
<td></td>
<td>0.481706</td>
<td>0.501860</td>
<td>0.481040</td>
<td>0.501172</td>
<td>0.000666</td>
<td>0.000688</td>
</tr>
<tr>
<td><inline-formula id="ieqn-46"><mml:math id="mml-ieqn-46"><mml:mi>&#x03C0;</mml:mi><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mn>3</mml:mn></mml:math></inline-formula></td>
<td></td>
<td></td>
<td></td>
<td>0.485708</td>
<td>0.505998</td>
<td>0.486320</td>
<td>0.506630</td>
<td>&#x2212;0.000612</td>
<td>&#x2212;0.000632</td>
</tr>
<tr>
<td><inline-formula id="ieqn-47"><mml:math id="mml-ieqn-47"><mml:mi>&#x03C0;</mml:mi><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mn>2</mml:mn></mml:math></inline-formula></td>
<td></td>
<td></td>
<td></td>
<td>0.477685</td>
<td>0.514217</td>
<td>0.493462</td>
<td>0.514013</td>
<td>&#x2212;0.015777</td>
<td>0.000204</td>
</tr>
<tr>
<td></td>
<td>0.1</td>
<td></td>
<td></td>
<td>0.470199</td>
<td>0.489964</td>
<td>0.4702023</td>
<td>0.4899674</td>
<td>&#x2212;3.3E&#x2212;06</td>
<td>&#x2212;3.4E&#x2212;06</td>
</tr>
<tr>
<td></td>
<td>0.5</td>
<td></td>
<td></td>
<td>0.472634</td>
<td>0.492481</td>
<td>0.4726306</td>
<td>0.4924778</td>
<td>3.4E&#x2212;06</td>
<td>3.2E&#x2212;06</td>
</tr>
<tr>
<td></td>
<td>0.9</td>
<td></td>
<td></td>
<td>0.475062</td>
<td>0.494992</td>
<td>0.4750589</td>
<td>0.4949882</td>
<td>3.1E&#x2212;06</td>
<td>3.8E&#x2212;06</td>
</tr>
<tr>
<td></td>
<td>1.3</td>
<td></td>
<td></td>
<td>0.477484</td>
<td>0.497495</td>
<td>0.4774872</td>
<td>0.4974986</td>
<td>&#x2212;3.2E&#x2212;06</td>
<td>&#x2212;3.6E&#x2212;06</td>
</tr>
<tr>
<td></td>
<td></td>
<td>0.5</td>
<td></td>
<td>0.674987</td>
<td>0.702228</td>
<td>0.6930934</td>
<td>0.721113</td>
<td>&#x2212;0.0181064</td>
<td>&#x2212;0.018885</td>
</tr>
<tr>
<td></td>
<td></td>
<td>1</td>
<td></td>
<td>0.955112</td>
<td>0.991836</td>
<td>0.9359903</td>
<td>0.9718615</td>
<td>0.0191217</td>
<td>0.0199745</td>
</tr>
<tr>
<td></td>
<td></td>
<td>1.5</td>
<td></td>
<td>1.194963</td>
<td>1.239316</td>
<td>1.1788872</td>
<td>1.2226100</td>
<td>0.0160758</td>
<td>0.016706</td>
</tr>
<tr>
<td></td>
<td></td>
<td>2</td>
<td></td>
<td>1.404693</td>
<td>1.455563</td>
<td>1.4217841</td>
<td>1.4733585</td>
<td>&#x2212;0.0170911</td>
<td>&#x2212;0.0177955</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td>0.2</td>
<td>0.354570</td>
<td>0.370268</td>
<td>0.35457</td>
<td>0.3776652</td>
<td>0</td>
<td>&#x2212;0.0073972</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td>0.4</td>
<td>0.481706</td>
<td>0.501860</td>
<td>0.481706</td>
<td>0.4940339</td>
<td>0</td>
<td>0.0078261</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td>0.6</td>
<td>0.593109</td>
<td>0.616942</td>
<td>0.593109</td>
<td>0.6104026</td>
<td>0</td>
<td>0.0065394</td>
</tr>
<tr>
<td></td>
<td></td>
<td></td>
<td>0.8</td>
<td>0.692774</td>
<td>0.719803</td>
<td>0.692774</td>
<td>0.7267713</td>
<td>0</td>
<td>&#x2212;0.0069683</td>
</tr>
</tbody>
</table>
</table-wrap><table-wrap id="table-4">
<label>Table 4</label>
<caption>
<title>Comparison of present study results with previous study results for <inline-formula id="ieqn-48"><mml:math id="mml-ieqn-48"><mml:msub><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mi>G</mml:mi><mml:mi>O</mml:mi></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:msub><mml:mi>&#x03D5;</mml:mi><mml:mrow><mml:mi>M</mml:mi><mml:mi>O</mml:mi><mml:mrow><mml:msub><mml:mi>S</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:mrow></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:mn>0</mml:mn></mml:math></inline-formula> with specific conditions</title>
</caption>
<table>
<colgroup>
<col align="center"/>
<col align="center"/>
<col align="center"/> </colgroup>
<thead>
<tr>
<th><inline-formula id="ieqn-49"><mml:math id="mml-ieqn-49"><mml:mi>X</mml:mi></mml:math></inline-formula></th>
<th>Gowtham et al. [<xref ref-type="bibr" rid="ref-37">37</xref>]</th>
<th>Present study</th>
</tr>
</thead>
<tbody>
<tr>
<td>0</td>
<td>0.640054</td>
<td>0.641502</td>
</tr>
<tr>
<td>0.2</td>
<td>0.661050</td>
<td>0.662051</td>
</tr>
<tr>
<td>0.4</td>
<td>0.700594</td>
<td>0.701595</td>
</tr>
<tr>
<td>0.6</td>
<td>0.762242</td>
<td>0.763645</td>
</tr>
<tr>
<td>0.8</td>
<td>0.86673</td>
<td>0.867721</td>
</tr>
<tr>
<td>1</td>
<td>1</td>
<td>1</td>
</tr>
</tbody>
</table>
</table-wrap><fig id="fig-1">
<label>Figure 1</label>
<caption>
<title>Applications of the current research</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-1.tif"/>
</fig><fig id="fig-2">
<label>Figure 2</label>
<caption>
<title>Schematic representation of the trapezoidal and rectangular fin</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-2.tif"/>
</fig><fig id="fig-3">
<label>Figure 3</label>
<caption>
<title>Gradient descent algorithm flow chart</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-3.tif"/>
</fig><fig id="fig-4">
<label>Figure 4</label>
<caption>
<title>Methodology of the present study</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-4.tif"/>
</fig>
<sec id="s4_1">
<label>4.1</label>
<title>Temperature Profiles for Various Parameters and Error Analysis</title>
<p>From <xref ref-type="fig" rid="fig-5">Fig. 5</xref> it is evident that as the wet porous parameter <inline-formula id="ieqn-50"><mml:math id="mml-ieqn-50"><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> improves from 0.2 to 0.8, both rectangular and trapezoidal fins exhibit faster deterioration in temperature along the fin length. Rectangular fin retains a higher temperature compared to a trapezoidal one, indicating a lower heat transfer rate. Thermal performance is better in trapezoidal due to its tapered geometry and the efficient surface area utilisation. <xref ref-type="fig" rid="fig-6">Fig. 6</xref> illustrates the absolute error for the variation in wet porous parameter <inline-formula id="ieqn-51"><mml:math id="mml-ieqn-51"><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> on temperature <inline-formula id="ieqn-52"><mml:math id="mml-ieqn-52"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula>. Both fin types exhibit similar error trends. From the plot, it is evident that the absolute error is very small; most of the error increase in <inline-formula id="ieqn-53"><mml:math id="mml-ieqn-53"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula> is less than 10<sup>&#x2212;8</sup>. Even the largest error is less than 10<sup>&#x2212;5</sup>. Such a low magnitude error confirms the model is numerically stable and robust for engineering applications. <xref ref-type="fig" rid="fig-7">Fig. 7</xref> illustrates that as the porosity parameter <inline-formula id="ieqn-54"><mml:math id="mml-ieqn-54"><mml:mrow><mml:mo>(</mml:mo><mml:mi>S</mml:mi><mml:mi>h</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> improves from 0.1 to 1.3, the temperature profiles <inline-formula id="ieqn-55"><mml:math id="mml-ieqn-55"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> decrease along the fin length. Higher porosity strengthens the fluid-solid interaction and thereby supports the convective heat transfer. Consequently, fin dissipates heat more effectively throughout its length. Rectangular fin consistently preserves a higher temperature compared to trapezoidal fin, exhibiting tapered geometry endorses greater heat transfer. <xref ref-type="fig" rid="fig-8">Fig. 8</xref> demonstrates the absolute error for the corresponding variation in <inline-formula id="ieqn-56"><mml:math id="mml-ieqn-56"><mml:mi>S</mml:mi><mml:mi>h</mml:mi></mml:math></inline-formula> on temperature <inline-formula id="ieqn-57"><mml:math id="mml-ieqn-57"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula>. The absolute error varies from 10<sup>&#x2212;12</sup> from the base to 10<sup>&#x2212;8</sup> at the tip of the fin, which is extremely small. Even the largest error value is below 10<sup>&#x2212;8</sup>, displaying computational model remains numerically accurate and reliable. The trapezoidal fin exhibits slightly higher absolute error compared with the rectangular fin because of its geometry, having a variable cross-sectional area. <xref ref-type="fig" rid="fig-9">Fig. 9</xref> illustrates the gradual loss of heat as a result of radiation and conduction throughout the length of the fin for different values of radiative parameter <inline-formula id="ieqn-58"><mml:math id="mml-ieqn-58"><mml:mrow><mml:mo>(</mml:mo><mml:mi>N</mml:mi><mml:mi>r</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> from 0.5 to 2. Compared to the trapezoidal fin, the rectangular fin has a higher temperature, because of its shape, the trapezoidal fin benefits more. <xref ref-type="fig" rid="fig-10">Fig. 10</xref> portrays the absolute error for the temperature distribution <inline-formula id="ieqn-59"><mml:math id="mml-ieqn-59"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> for the corresponding variation in <inline-formula id="ieqn-60"><mml:math id="mml-ieqn-60"><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula>. The absolute error is relatively small, ranging from 10<sup>&#x2212;12</sup> to 10<sup>&#x2212;6</sup> for all the cases. This confirms the precision of the numerical model. <xref ref-type="fig" rid="fig-11">Fig. 11</xref> depicts the variation <inline-formula id="ieqn-61"><mml:math id="mml-ieqn-61"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> along the fin length for different inclination angle values <inline-formula id="ieqn-62"><mml:math id="mml-ieqn-62"><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C4;</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> for both trapezoidal and rectangular fins. As <inline-formula id="ieqn-63"><mml:math id="mml-ieqn-63"><mml:msup><mml:mi>T</mml:mi><mml:mrow><mml:mo>&#x2217;</mml:mo></mml:mrow></mml:msup></mml:math></inline-formula> increases from <inline-formula id="ieqn-64"><mml:math id="mml-ieqn-64"><mml:msup><mml:mn>30</mml:mn><mml:mrow><mml:mn>0</mml:mn></mml:mrow></mml:msup></mml:math></inline-formula> to <inline-formula id="ieqn-65"><mml:math id="mml-ieqn-65"><mml:msup><mml:mn>90</mml:mn><mml:mrow><mml:mn>0</mml:mn></mml:mrow></mml:msup></mml:math></inline-formula>, <inline-formula id="ieqn-66"><mml:math id="mml-ieqn-66"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> declines along the fin length. Fins at larger inclination angles dissipate more heat and lower fin temperature. The trapezoidal fin, due to its tapered profile, consistently exhibits lower values <inline-formula id="ieqn-67"><mml:math id="mml-ieqn-67"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> than a rectangular fin. <xref ref-type="fig" rid="fig-12">Fig. 12</xref> represents the absolute error for the temperature distribution <inline-formula id="ieqn-68"><mml:math id="mml-ieqn-68"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> for the corresponding variation in <inline-formula id="ieqn-69"><mml:math id="mml-ieqn-69"><mml:msup><mml:mi>T</mml:mi><mml:mrow><mml:mo>&#x2217;</mml:mo></mml:mrow></mml:msup></mml:math></inline-formula>. Extremely low magnitude error (below 10<sup>&#x2212;7</sup>) confirms robustness and high accuracy of the computational approach. The rectangular fin exhibits consistently low absolute error compared to the trapezoidal fin.</p>
<fig id="fig-5">
<label>Figure 5</label>
<caption>
<title>Plot of <inline-formula id="ieqn-70"><mml:math id="mml-ieqn-70"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:mspace width="thinmathspace" /><mml:mrow><mml:mtext>vs.</mml:mtext></mml:mrow><mml:mspace width="thinmathspace" /><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-5.tif"/>
</fig><fig id="fig-6">
<label>Figure 6</label>
<caption>
<title>Absolute error of <inline-formula id="ieqn-89"><mml:math id="mml-ieqn-89"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> for <inline-formula id="ieqn-90"><mml:math id="mml-ieqn-90"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-6.tif"/>
</fig><fig id="fig-7">
<label>Figure 7</label>
<caption>
<title>Plot of <inline-formula id="ieqn-91"><mml:math id="mml-ieqn-91"><mml:mi>S</mml:mi><mml:mi>h</mml:mi><mml:mi>v</mml:mi><mml:mi>s</mml:mi><mml:mo>.</mml:mo><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-7.tif"/>
</fig><fig id="fig-8">
<label>Figure 8</label>
<caption>
<title>Absolute error of <inline-formula id="ieqn-92"><mml:math id="mml-ieqn-92"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> for <inline-formula id="ieqn-93"><mml:math id="mml-ieqn-93"><mml:mi>S</mml:mi><mml:mi>h</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-8.tif"/>
</fig><fig id="fig-9">
<label>Figure 9</label>
<caption>
<title>Plot of <inline-formula id="ieqn-94"><mml:math id="mml-ieqn-94"><mml:mi>N</mml:mi><mml:mi>r</mml:mi><mml:mspace width="thinmathspace" /><mml:mrow><mml:mtext>vs.</mml:mtext></mml:mrow><mml:mspace width="thinmathspace" /><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-9.tif"/>
</fig><fig id="fig-10">
<label>Figure 10</label>
<caption>
<title>Absolute error of <inline-formula id="ieqn-95"><mml:math id="mml-ieqn-95"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> for <inline-formula id="ieqn-96"><mml:math id="mml-ieqn-96"><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-10.tif"/>
</fig><fig id="fig-11">
<label>Figure 11</label>
<caption>
<title>Plot of <inline-formula id="ieqn-97"><mml:math id="mml-ieqn-97"><mml:mi>&#x03C4;</mml:mi><mml:mi>v</mml:mi><mml:mi>s</mml:mi><mml:mo>.</mml:mo><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-11.tif"/>
</fig><fig id="fig-12">
<label>Figure 12</label>
<caption>
<title>Absolute error of <inline-formula id="ieqn-98"><mml:math id="mml-ieqn-98"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> for <inline-formula id="ieqn-99"><mml:math id="mml-ieqn-99"><mml:mi>&#x03C4;</mml:mi></mml:math></inline-formula></title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-12.tif"/>
</fig>
</sec>
<sec id="s4_2">
<label>4.2</label>
<title>Surface and Contour Plots</title>
<p>The surface and contour plots in <xref ref-type="fig" rid="fig-13">Figs. 13</xref> and <xref ref-type="fig" rid="fig-14">14</xref> explain the decline in temperature <inline-formula id="ieqn-71"><mml:math id="mml-ieqn-71"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> for the corresponding increase in fin length and angle of inclination <inline-formula id="ieqn-72"><mml:math id="mml-ieqn-72"><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C4;</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> for the rectangular fin, due to conductive-convective heat transfer. The consistent contours and even gradients validate the numerical model&#x2019;s accuracy and stability. The results are useful for designing heat exchangers, electronic cooling systems, solar thermal devices, and radiators, where the proper selection of inclination angle and fin geometry can substantially augment heat transfer. <xref ref-type="fig" rid="fig-15">Figs. 15</xref> and <xref ref-type="fig" rid="fig-16">16</xref> illustrate the decrease in temperature <inline-formula id="ieqn-73"><mml:math id="mml-ieqn-73"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> with an increment in wet porous parameter <inline-formula id="ieqn-74"><mml:math id="mml-ieqn-74"><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> and fin length for the rectangular fin. This decline corresponds to enhanced convective heat transfer within the porous medium. The obtained results are useful in the design of moisture-based cooling systems and porous heat exchangers, where optimized porosity and fin geometry can substantially enhance energy efficiency and thermal performance. A noticeable temperature <inline-formula id="ieqn-75"><mml:math id="mml-ieqn-75"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> decline is observed due to the combined increase in fin length and radiative parameter <inline-formula id="ieqn-76"><mml:math id="mml-ieqn-76"><mml:mrow><mml:mo>(</mml:mo><mml:mi>N</mml:mi><mml:mi>r</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> for the rectangular fin from <xref ref-type="fig" rid="fig-17">Figs. 17</xref> and <xref ref-type="fig" rid="fig-18">18</xref>. Stronger <inline-formula id="ieqn-77"><mml:math id="mml-ieqn-77"><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula> corresponds to greater heat loss from the fin surface. The obtained results are significant for the design of high temperature fins, radiators, space thermal control systems, solar absorbers etc. where radiation has a dominant role in overall heat transfer. <xref ref-type="fig" rid="fig-19">Figs. 19</xref> and <xref ref-type="fig" rid="fig-20">20</xref> demonstrate a progressive decrease in temperature <inline-formula id="ieqn-78"><mml:math id="mml-ieqn-78"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> for the rectangular fin with the improving porosity parameter <inline-formula id="ieqn-79"><mml:math id="mml-ieqn-79"><mml:mrow><mml:mo>(</mml:mo><mml:mi>S</mml:mi><mml:mi>h</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> and the fin length. This is because higher porosity enhances convective heat transfer within the fin material by allowing greater hybrid fluid penetration and interaction. Practically the results are valuable for optimizing the design of catalytic converters, electronic cooling modules and porous heat exchangers. The surface and contour plots, <xref ref-type="fig" rid="fig-21">Figs. 21</xref> and <xref ref-type="fig" rid="fig-22">22</xref> depict a decline in temperature <inline-formula id="ieqn-80"><mml:math id="mml-ieqn-80"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> with the corresponding increase in fin length and angle of inclination <inline-formula id="ieqn-81"><mml:math id="mml-ieqn-81"><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C4;</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> for the trapezoidal fin. This trend arises due to conductive-convective heat transfer. The results suggest that appropriate adjustment of fin geometry and inclination can improve electronic cooling systems, compact heat exchangers, and solar air heaters&#x2019; thermal efficiency. <xref ref-type="fig" rid="fig-23">Figs. 23</xref> and <xref ref-type="fig" rid="fig-24">24</xref> represent the temperature distribution <inline-formula id="ieqn-82"><mml:math id="mml-ieqn-82"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> is decreasing progressively in a trapezoidal fin due to the combined rise in wet porous parameter <inline-formula id="ieqn-83"><mml:math id="mml-ieqn-83"><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> and the fin length. Higher values of <inline-formula id="ieqn-84"><mml:math id="mml-ieqn-84"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula> enhance convective heat transfer within the porous medium thereby promote improved heat dissipation from the fin&#x2019;s surface. From <xref ref-type="fig" rid="fig-25">Figs. 25</xref> and <xref ref-type="fig" rid="fig-26">26</xref>, it is evident that the temperature distribution <inline-formula id="ieqn-85"><mml:math id="mml-ieqn-85"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> declines in trapezoidal fin with the rise in both radiation and fin length. Rise in <inline-formula id="ieqn-86"><mml:math id="mml-ieqn-86"><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula> facilitates greater energy dissipation from the fin surface. The result is applicable to engineering applications such heat exchangers, gas turbines, and air conditioning, electronic component and solar thermal collectors where radiation plays a vital role in thermal management. <xref ref-type="fig" rid="fig-27">Figs. 27</xref> and <xref ref-type="fig" rid="fig-28">28</xref> demonstrate a progressive decrease in temperature <inline-formula id="ieqn-87"><mml:math id="mml-ieqn-87"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> for the trapezoidal fin with the improving porosity parameter <inline-formula id="ieqn-88"><mml:math id="mml-ieqn-88"><mml:mrow><mml:mo>(</mml:mo><mml:mi>S</mml:mi><mml:mi>h</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> and the fin length. An increase in porosity substantially promotes fluid permeability within the fin material; consequently, convective heat transfer is improved. These findings are extremely pertinent to engineering applications like small cooling devices and porous heat exchangers, among others.</p>
<fig id="fig-13">
<label>Figure 13</label>
<caption>
<title>Surface plot of <inline-formula id="ieqn-100"><mml:math id="mml-ieqn-100"><mml:mi>&#x03B8;</mml:mi></mml:math></inline-formula> for <inline-formula id="ieqn-101"><mml:math id="mml-ieqn-101"><mml:mi>&#x03C4;</mml:mi></mml:math></inline-formula> in rectangular fin case</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-13.tif"/>
</fig><fig id="fig-14">
<label>Figure 14</label>
<caption>
<title>Contour plot of <inline-formula id="ieqn-102"><mml:math id="mml-ieqn-102"><mml:mi>&#x03B8;</mml:mi></mml:math></inline-formula> for <inline-formula id="ieqn-103"><mml:math id="mml-ieqn-103"><mml:mi>&#x03C4;</mml:mi></mml:math></inline-formula> in rectangular fin case</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-14.tif"/>
</fig><fig id="fig-15">
<label>Figure 15</label>
<caption>
<title>Surface plot of <inline-formula id="ieqn-104"><mml:math id="mml-ieqn-104"><mml:mi>&#x03B8;</mml:mi></mml:math></inline-formula> for <inline-formula id="ieqn-105"><mml:math id="mml-ieqn-105"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula> in rectangular fin case</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-15.tif"/>
</fig><fig id="fig-16">
<label>Figure 16</label>
<caption>
<title>Contour plot of <inline-formula id="ieqn-106"><mml:math id="mml-ieqn-106"><mml:mi>&#x03B8;</mml:mi></mml:math></inline-formula> for <inline-formula id="ieqn-107"><mml:math id="mml-ieqn-107"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula> in rectangular fin case</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-16.tif"/>
</fig><fig id="fig-17">
<label>Figure 17</label>
<caption>
<title>Surface plot of <inline-formula id="ieqn-108"><mml:math id="mml-ieqn-108"><mml:mi>&#x03B8;</mml:mi></mml:math></inline-formula> for <inline-formula id="ieqn-109"><mml:math id="mml-ieqn-109"><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula> in rectangular fin case</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-17.tif"/>
</fig><fig id="fig-18">
<label>Figure 18</label>
<caption>
<title>Contour plot of <inline-formula id="ieqn-110"><mml:math id="mml-ieqn-110"><mml:mi>&#x03B8;</mml:mi></mml:math></inline-formula> for <inline-formula id="ieqn-111"><mml:math id="mml-ieqn-111"><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula> in rectangular fin case</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-18.tif"/>
</fig><fig id="fig-19">
<label>Figure 19</label>
<caption>
<title>Surface plot of <inline-formula id="ieqn-112"><mml:math id="mml-ieqn-112"><mml:mi>&#x03B8;</mml:mi></mml:math></inline-formula> for <inline-formula id="ieqn-113"><mml:math id="mml-ieqn-113"><mml:mi>S</mml:mi><mml:mi>h</mml:mi></mml:math></inline-formula> in rectangular fin case</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-19.tif"/>
</fig><fig id="fig-20">
<label>Figure 20</label>
<caption>
<title>Contour plot of <inline-formula id="ieqn-114"><mml:math id="mml-ieqn-114"><mml:mi>&#x03B8;</mml:mi></mml:math></inline-formula> for <inline-formula id="ieqn-115"><mml:math id="mml-ieqn-115"><mml:mi>S</mml:mi><mml:mi>h</mml:mi></mml:math></inline-formula> in rectangular fin case</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-20.tif"/>
</fig><fig id="fig-21">
<label>Figure 21</label>
<caption>
<title>Surface plot of <inline-formula id="ieqn-116"><mml:math id="mml-ieqn-116"><mml:mi>&#x03B8;</mml:mi></mml:math></inline-formula> for <inline-formula id="ieqn-117"><mml:math id="mml-ieqn-117"><mml:mi>&#x03C4;</mml:mi></mml:math></inline-formula> in trapezoidal fin case</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-21.tif"/>
</fig><fig id="fig-22">
<label>Figure 22</label>
<caption>
<title>Contour plot of <inline-formula id="ieqn-118"><mml:math id="mml-ieqn-118"><mml:mi>&#x03B8;</mml:mi></mml:math></inline-formula> for <inline-formula id="ieqn-119"><mml:math id="mml-ieqn-119"><mml:mi>&#x03C4;</mml:mi></mml:math></inline-formula> in trapezoidal fin case</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-22.tif"/>
</fig><fig id="fig-23">
<label>Figure 23</label>
<caption>
<title>Surface plot of <inline-formula id="ieqn-120"><mml:math id="mml-ieqn-120"><mml:mi>&#x03B8;</mml:mi></mml:math></inline-formula> for <inline-formula id="ieqn-121"><mml:math id="mml-ieqn-121"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula> in trapezoidal fin case</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-23.tif"/>
</fig><fig id="fig-24">
<label>Figure 24</label>
<caption>
<title>Contour plot of <inline-formula id="ieqn-122"><mml:math id="mml-ieqn-122"><mml:mi>&#x03B8;</mml:mi></mml:math></inline-formula> for <inline-formula id="ieqn-123"><mml:math id="mml-ieqn-123"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula> in trapezoidal fin case</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-24.tif"/>
</fig><fig id="fig-25">
<label>Figure 25</label>
<caption>
<title>Surface plot of <inline-formula id="ieqn-124"><mml:math id="mml-ieqn-124"><mml:mi>&#x03B8;</mml:mi></mml:math></inline-formula> for <inline-formula id="ieqn-125"><mml:math id="mml-ieqn-125"><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula> in trapezoidal fin case</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-25.tif"/>
</fig><fig id="fig-26">
<label>Figure 26</label>
<caption>
<title>Contour plot of <inline-formula id="ieqn-126"><mml:math id="mml-ieqn-126"><mml:mi>&#x03B8;</mml:mi></mml:math></inline-formula> for <inline-formula id="ieqn-127"><mml:math id="mml-ieqn-127"><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula> in trapezoidal fin case</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-26.tif"/>
</fig><fig id="fig-27">
<label>Figure 27</label>
<caption>
<title>Surface plot of <inline-formula id="ieqn-128"><mml:math id="mml-ieqn-128"><mml:mi>&#x03B8;</mml:mi></mml:math></inline-formula> for <inline-formula id="ieqn-129"><mml:math id="mml-ieqn-129"><mml:mi>S</mml:mi><mml:mi>h</mml:mi></mml:math></inline-formula> in trapezoidal fin case</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-27.tif"/>
</fig><fig id="fig-28">
<label>Figure 28</label>
<caption>
<title>Contour plot of <inline-formula id="ieqn-130"><mml:math id="mml-ieqn-130"><mml:mi>&#x03B8;</mml:mi></mml:math></inline-formula> for <inline-formula id="ieqn-131"><mml:math id="mml-ieqn-131"><mml:mi>S</mml:mi><mml:mi>h</mml:mi></mml:math></inline-formula> in trapezoidal fin case</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-28.tif"/>
</fig>
</sec>
<sec id="s4_3">
<label>4.3</label>
<title>Gradient Descent Optimization</title>
<p>The outcomes of the optimisation algorithm based on the Gradient Descent method.</p>
<p><xref ref-type="fig" rid="fig-29">Fig. 29</xref> presents a linear fit plot of <inline-formula id="ieqn-132"><mml:math id="mml-ieqn-132"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula> for the rectangular fin and demonstrates a good correlation with R<sup>2</sup> &#x003D; 0.9970 with a low RMSE of 0.006882. This is a sign that there is great congruence between the predicted and observed values, and therefore, the fitted model was high in accuracy and reliability. <xref ref-type="fig" rid="fig-30">Fig. 30</xref> illustrates the linear fit plot of <inline-formula id="ieqn-133"><mml:math id="mml-ieqn-133"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula> for the trapezoidal fin, showing an excellent correlation with <inline-formula id="ieqn-134"><mml:math id="mml-ieqn-134"><mml:msup><mml:mi>R</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mo>=</mml:mo><mml:mn>0.9969</mml:mn></mml:math></inline-formula> and a low RMSE &#x003D; 0.007199. The close alignment between truth and fitted values confirms the high precision and reliability of the proposed model for trapezoidal fin performance prediction. The linear fit plot of <inline-formula id="ieqn-135"><mml:math id="mml-ieqn-135"><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula> is shown in <xref ref-type="fig" rid="fig-31">Fig. 31</xref> for the rectangular fin, a high linear relationship with <italic>R</italic><sup>2</sup> &#x003D; 0.9958 and a low RMSE of 0.01764 shows outcomes with good agreement between the truth values and the predictions. The linear fit plot of <inline-formula id="ieqn-136"><mml:math id="mml-ieqn-136"><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula> is represented in <xref ref-type="fig" rid="fig-32">Fig. 32</xref> in the case of the trapezoidal fin, showing a very good linear correlation with <italic>R</italic><sup>2</sup> &#x003D; 0.9957 and a low RMSE of 0.01838. The fitted data are almost the same assures the validity and precision of the model for forecasting the trapezoidal fin&#x2019;s thermal performance. The plot of the linear fit of <inline-formula id="ieqn-137"><mml:math id="mml-ieqn-137"><mml:mi>S</mml:mi><mml:mi>h</mml:mi></mml:math></inline-formula> is indicated in <xref ref-type="fig" rid="fig-33">Fig. 33</xref> for the rectangular fin, which shows a perfect correlation with <italic>R</italic><sup>2</sup> &#x003D; 1 and an extremely low RMSE of 3.2517e&#x2212;06. This signifies that there is an ideal linear relationship between which proves the outstanding accuracy and stability of the model for the rectangular fin thermal analysis. The linear fit plot of <inline-formula id="ieqn-138"><mml:math id="mml-ieqn-138"><mml:mi>S</mml:mi><mml:mi>h</mml:mi></mml:math></inline-formula> for the trapezoidal fin is plotted in <xref ref-type="fig" rid="fig-34">Fig. 34</xref>, and the linear relationship with <italic>R</italic><sup>2</sup> &#x003D; 1 and a very low RMSE of 3.507e&#x2212;06. This shows an excellent fit between the anticipated and real data, demonstrating the model&#x2019;s accuracy and dependability for the trapezoidal fin thermal analysis. <xref ref-type="fig" rid="fig-35">Fig. 35</xref> depicts the linear regression graph of <inline-formula id="ieqn-139"><mml:math id="mml-ieqn-139"><mml:mi>&#x03C4;</mml:mi></mml:math></inline-formula> very strong correlation is observed with <italic>R</italic><sup>2</sup> &#x003D; 0.9934 and minimum RMSE &#x003D; 0.003322. The fact that the actual data and the fitted data confirm the validity and application of the linear model in estimating thermal behaviour in a rectangular fin. <xref ref-type="fig" rid="fig-36">Fig. 36</xref> illustrates the linear fit plot of <inline-formula id="ieqn-140"><mml:math id="mml-ieqn-140"><mml:mi>&#x03C4;</mml:mi></mml:math></inline-formula> with a strong correlation in the trapezoidal fin case with <italic>R</italic><sup>2</sup> &#x003D; 0.9934 and a very low RMSE of 1.656e&#x2212;05. The high ability of the proposed linear model with a good fit guarantees accurate prediction of the trapezoidal fin&#x2019;s thermal performance. This indicates a strong linear dependence of the temperature distribution <inline-formula id="ieqn-141"><mml:math id="mml-ieqn-141"><mml:mi>&#x03B8;</mml:mi><mml:mrow><mml:mo>(</mml:mo><mml:mi>X</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> on the governing parameters with ranges <inline-formula id="ieqn-142"><mml:math id="mml-ieqn-142"><mml:mrow><mml:mo>(</mml:mo><mml:mfrac><mml:mi>&#x03C0;</mml:mi><mml:mn>6</mml:mn></mml:mfrac><mml:mo>&#x2264;</mml:mo><mml:mi>&#x03C4;</mml:mi><mml:mo>&#x2264;</mml:mo><mml:mfrac><mml:mi>&#x03C0;</mml:mi><mml:mn>2</mml:mn></mml:mfrac><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula>, <inline-formula id="ieqn-143"><mml:math id="mml-ieqn-143"><mml:mrow><mml:mo>(</mml:mo><mml:mn>0.2</mml:mn><mml:mo>&#x2264;</mml:mo><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:mo>&#x2264;</mml:mo><mml:mn>0.8</mml:mn><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula>, <inline-formula id="ieqn-144"><mml:math id="mml-ieqn-144"><mml:mrow><mml:mo>(</mml:mo><mml:mn>0.1</mml:mn><mml:mo>&#x2264;</mml:mo><mml:mi>S</mml:mi><mml:mi>h</mml:mi><mml:mo>&#x2264;</mml:mo><mml:mn>1.3</mml:mn><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula>, and <inline-formula id="ieqn-145"><mml:math id="mml-ieqn-145"><mml:mrow><mml:mo>(</mml:mo><mml:mn>0.5</mml:mn><mml:mo>&#x2264;</mml:mo><mml:mi>N</mml:mi><mml:mi>r</mml:mi><mml:mo>&#x2264;</mml:mo><mml:mn>2</mml:mn><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> for both trapezoidal and rectangular fin.</p>
<fig id="fig-29">
<label>Figure 29</label>
<caption>
<title>Fit Plot of <inline-formula id="ieqn-146"><mml:math id="mml-ieqn-146"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula> for rectangular fin</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-29.tif"/>
</fig><fig id="fig-30">
<label>Figure 30</label>
<caption>
<title>Fit Plot of <inline-formula id="ieqn-149"><mml:math id="mml-ieqn-149"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula> for trapezoidal fin</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-30.tif"/>
</fig><fig id="fig-31">
<label>Figure 31</label>
<caption>
<title>Fit Plot of <inline-formula id="ieqn-150"><mml:math id="mml-ieqn-150"><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula> for rectangular fin</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-31.tif"/>
</fig><fig id="fig-32">
<label>Figure 32</label>
<caption>
<title>Fit Plot of <inline-formula id="ieqn-151"><mml:math id="mml-ieqn-151"><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula> for trapezoidal fin</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-32.tif"/>
</fig><fig id="fig-33">
<label>Figure 33</label>
<caption>
<title>Fit Plot of <inline-formula id="ieqn-152"><mml:math id="mml-ieqn-152"><mml:mi>S</mml:mi><mml:mi>h</mml:mi></mml:math></inline-formula> for rectangular fin</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-33.tif"/>
</fig><fig id="fig-34">
<label>Figure 34</label>
<caption>
<title>Fit Plot of <inline-formula id="ieqn-153"><mml:math id="mml-ieqn-153"><mml:mi>S</mml:mi><mml:mi>h</mml:mi></mml:math></inline-formula> for trapezoidal fin</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-34.tif"/>
</fig><fig id="fig-35">
<label>Figure 35</label>
<caption>
<title>Fit Plot of <inline-formula id="ieqn-154"><mml:math id="mml-ieqn-154"><mml:mi>&#x03C4;</mml:mi></mml:math></inline-formula> for rectangular fin</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-35.tif"/>
</fig><fig id="fig-36">
<label>Figure 36</label>
<caption>
<title>Fit Plot of <inline-formula id="ieqn-155"><mml:math id="mml-ieqn-155"><mml:mi>&#x03C4;</mml:mi></mml:math></inline-formula> for trapezoidal fin</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-36.tif"/>
</fig>
</sec>
<sec id="s4_4">
<label>4.4</label>
<title>Sensitivity Analysis</title>
<p>A variance-based technique for global sensitivity analysis, Sobol sensitivity analysis calculates the degree to which each input parameter <inline-formula id="ieqn-147"><mml:math id="mml-ieqn-147"><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C4;</mml:mi><mml:mo>,</mml:mo><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:mo>,</mml:mo><mml:mi>S</mml:mi><mml:mi>h</mml:mi><mml:mo>,</mml:mo><mml:mi>N</mml:mi><mml:mi>r</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> and its interactions affect the overall variance of a model&#x2019;s output <inline-formula id="ieqn-148"><mml:math id="mml-ieqn-148"><mml:mrow><mml:mo>(</mml:mo><mml:mrow><mml:mtext>Heat Transfer</mml:mtext></mml:mrow><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula>. The total effect indices are used to account for the direct and indirect influence of a parameter, and the total output variance is broken down into fractions attributable to individual inputs (first-order indices) and combinations of inputs (higher-order indices). This approach helps discover important drivers in a complicated system by determining which parameters have the most influence. The results of the Rectangular Fin case&#x2019;s Sobel Sensitivity Analysis are shown in <xref ref-type="fig" rid="fig-37">Fig. 37</xref> with the first-order (S1) and total-order (ST) indices with the 95% confidence interval. The ST values of 1, 2, and 4 are very high (around 0.96&#x2013;0.98), and this proves that the impact is overall strong, whereas the ST of Input 3 is rather high (S1 &#x003D; 0.72), which means that it significantly influences the output. The Sobel Sensitivity Analysis results for the Trapezoidal Fin case are shown in <xref ref-type="fig" rid="fig-38">Fig. 38</xref> in colour-enhanced bars. The ST indices (pink) of the inputs of 1, 2 and 4 are close to 0.97&#x2013;0.98, representing the overall influence, whereas the highest S1 is found with the input of 3 (0.75), representing the strongest direct impact on the model output.</p>
<fig id="fig-37">
<label>Figure 37</label>
<caption>
<title>Sensitivity analysis plot for rectangular fin case</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-37.tif"/>
</fig><fig id="fig-38">
<label>Figure 38</label>
<caption>
<title>Sensitivity analysis plot for trapezoidal fin cas</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-38.tif"/>
</fig>
</sec>
<sec id="s4_5">
<label>4.5</label>
<title>Stability Analysis and Grid Independence Test</title>
<p><xref ref-type="fig" rid="fig-39">Fig. 39</xref> shows that the results for both the medium and fine meshes agree in the rectangular and trapezoidal cases, indicating that the current study meets the criteria for grid independence testing. <xref ref-type="fig" rid="fig-40">Fig. 40</xref> depicts a linear rise in heat transfer with the parameter <inline-formula id="ieqn-156"><mml:math id="mml-ieqn-156"><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula>, which means a predictable and stable relationship. The fitted line <inline-formula id="ieqn-157"><mml:math id="mml-ieqn-157"><mml:mi>Q</mml:mi><mml:mo>=</mml:mo><mml:mn>0.450</mml:mn><mml:mo>+</mml:mo><mml:mn>0.486</mml:mn><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula> comes close to the data points, and all values lie within specification limits and hence, good numerical stability for the rectangular fin case. <xref ref-type="fig" rid="fig-41">Fig. 41</xref> represents a sharp linear growth in heat transfer with the parameter <inline-formula id="ieqn-158"><mml:math id="mml-ieqn-158"><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula> passing through the fitted line, <inline-formula id="ieqn-159"><mml:math id="mml-ieqn-159"><mml:mi>Q</mml:mi><mml:mo>=</mml:mo><mml:mn>0.470</mml:mn><mml:mo>+</mml:mo><mml:mn>0.501</mml:mn><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula> forecasts are close to the data points, and they are within the specification limits, meaning that the trapezoidal fin case displays stable, reliable numeric behaviour.</p>
<fig id="fig-39">
<label>Figure 39</label>
<caption>
<title>Grid independence test</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-39.tif"/>
</fig><fig id="fig-40">
<label>Figure 40</label>
<caption>
<title>Numerical stability analysis for the rectangular fin</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-40.tif"/>
</fig><fig id="fig-41">
<label>Figure 41</label>
<caption>
<title>Numerical stability analysis for the trapezoidal fin</title>
</caption>
<graphic mimetype="image" mime-subtype="tif" xlink:href="CMES_74680-fig-41.tif"/>
</fig>
</sec>
</sec>
<sec id="s5">
<label>5</label>
<title>Conclusion</title>
<p>The thermal behaviour of a wetted hybrid nanofluid with inclined trapezoidal and rectangular porous fins was investigated in this work in MATLAB software with the Lobatto IIIa collocation method using the BVP5C solver to examine the impact of the inclination angle <inline-formula id="ieqn-160"><mml:math id="mml-ieqn-160"><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C4;</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula>, parameter for wet porous <inline-formula id="ieqn-161"><mml:math id="mml-ieqn-161"><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula>, porosity parameter <inline-formula id="ieqn-162"><mml:math id="mml-ieqn-162"><mml:mrow><mml:mo>(</mml:mo><mml:mi>S</mml:mi><mml:mi>h</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> and radiative parameter <inline-formula id="ieqn-163"><mml:math id="mml-ieqn-163"><mml:mrow><mml:mo>(</mml:mo><mml:mi>N</mml:mi><mml:mi>r</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> for both rectangular and trapezoidal fins, and Gradient Descent optimization applied to predict the heat transfer rate in rectangular and trapezoidal fins scenarios.</p>
<p><bold>Key Findings of the Present Study:</bold>
<list list-type="simple">
<list-item><label>&#x2756;</label><p>The temperature decreases progressively with the rise in the inclination angle <inline-formula id="ieqn-164"><mml:math id="mml-ieqn-164"><mml:mrow><mml:mo>(</mml:mo><mml:mi>&#x03C4;</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula>, parameter for wet porous <inline-formula id="ieqn-165"><mml:math id="mml-ieqn-165"><mml:mrow><mml:mo>(</mml:mo><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula>, porosity parameter <inline-formula id="ieqn-166"><mml:math id="mml-ieqn-166"><mml:mrow><mml:mo>(</mml:mo><mml:mi>S</mml:mi><mml:mi>h</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> and radiative parameter <inline-formula id="ieqn-167"><mml:math id="mml-ieqn-167"><mml:mrow><mml:mo>(</mml:mo><mml:mi>N</mml:mi><mml:mi>r</mml:mi><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula>, indicating substantial heat dissipation.</p></list-item>
<list-item><label>&#x2756;</label><p>Trapezoidal fin consistently exhibits better heat transfer mechanism than rectangular fin due to its tapered geometry.</p></list-item>
<list-item><label>&#x2756;</label><p>Due to the increased permeability and solid-fluid interaction within the fin, the wet porous parameter and porosity significantly lower the temperature of the hybrid nanofluid.</p></list-item>
<list-item><label>&#x2756;</label><p>Integrating both radiative and convective heat transfer leads to effective thermal performance.</p></list-item>
<list-item><label>&#x2756;</label><p>The absolute error remains extremely small 10<sup>&#x2212;12</sup>&#x2013;10<sup>&#x2212;6</sup>, validating that the adapted numerical method is highly accurate and stable.</p></list-item>
<list-item><label>&#x2756;</label><p>The linear regression results reveal excellent correlation between fitted and computed data, with R<sup>2</sup> values are <inline-formula id="ieqn-168"><mml:math id="mml-ieqn-168"><mml:mrow><mml:mo>(</mml:mo><mml:mo>&#x2248;</mml:mo><mml:mspace width="negativethinmathspace" /><mml:mn>1</mml:mn><mml:mo>)</mml:mo></mml:mrow></mml:math></inline-formula> confirming the consistency and reliability of the model.</p></list-item>
</list></p>
<p><bold>Limitations of the Present Study:</bold>
<list list-type="simple">
<list-item><label>&#x2756;</label><p>The present study examined a hybrid nanofluid only</p></list-item>
<list-item><label>&#x2756;</label><p>Comparison of results with experimental study</p></list-item>
<list-item><label>&#x2756;</label><p>In the present study, limited convective and radiative effects on heat transfer were considered.</p></list-item>
<list-item><label>&#x2756;</label><p>This study is limited to steady-state heat transfer</p></list-item>
</list></p>
<p><bold>Future Scope:</bold></p>
<p>To simplify the model, it was assumed that there was a perfect stationary state with homogeneous throughout flotation of the hybrid nanofluid. In the future, the aggregation, sedimentation and stability of nanoparticles will be taken into consideration with the aim of making the model have more practical considerations.</p>
</sec>
</body>
<back>
<ack>
<p>Not applicable.</p>
</ack>
<sec>
<title>Funding Statement</title>
<p>This research was supported by the &#x201C;Regional Innovation System &#x0026; Education (RISE)&#x201D; through the Seoul RISE Center, funded by the Ministry of Education (MOE) and the Seoul Metropolitan Government (2025-RISE-01-027-04).</p>
</sec>
<sec>
<title>Author Contributions</title>
<p>Maddina Dinesh Kumar: Writing&#x2014;original draft, Methodology, Resources, Software, Visualization, Validation. S. U. Mamatha: Writing&#x2014;original draft, Methodology, Investigation, Formal analysis. Khalid Masood: Validation, Conceptualization, Methodology, Formal analysis. Nehad Ali Shah: Investigation, Supervision, Formal analysis, Methodology, Conceptualisation. Se-Jin Yook: Writing&#x2014;review &#x0026; editing, Software, Supervision, Project administration. Maddina Dinesh Kumar and Nehad Ali Shah contributed equally to this work and are co-first authors. All authors reviewed the results and approved the final version of the manuscript.</p>
</sec>
<sec sec-type="data-availability">
<title>Availability of Data and Materials</title>
<p>Data will be available with the corresponding author on reasonable request.</p>
</sec>
<sec>
<title>Ethics Approval</title>
<p>Not applicable.</p>
</sec>
<sec sec-type="COI-statement">
<title>Conflicts of Interest</title>
<p>The authors declare no conflicts of interest to report regarding the present study.</p>
</sec>
<glossary content-type="abbreviations" id="glossary-1">
<title>Nomenclature</title>
<def-list>
<def-item>
<term>Symbol</term>
<def>
<p>Description SI units</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-169"><mml:math id="mml-ieqn-169"><mml:mi>A</mml:mi></mml:math></inline-formula></term>
<def>
<p>Fin cross-sectional area <inline-formula id="ieqn-170"><mml:math id="mml-ieqn-170"><mml:msup><mml:mrow><mml:mtext>m</mml:mtext></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-171"><mml:math id="mml-ieqn-171"><mml:msub><mml:mi>C</mml:mi><mml:mrow><mml:mi>p</mml:mi></mml:mrow></mml:msub></mml:math></inline-formula></term>
<def>
<p>Specific heat at constant pressure <inline-formula id="ieqn-172"><mml:math id="mml-ieqn-172"><mml:mrow><mml:mtext>J</mml:mtext></mml:mrow><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mrow><mml:mtext>kg</mml:mtext></mml:mrow><mml:mo>.</mml:mo><mml:mrow><mml:mtext>K</mml:mtext></mml:mrow></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-173"><mml:math id="mml-ieqn-173"><mml:msub><mml:mi>b</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula></term>
<def>
<p>Variable temperature <inline-formula id="ieqn-174"><mml:math id="mml-ieqn-174"><mml:mn>1</mml:mn><mml:mrow><mml:mo>/</mml:mo></mml:mrow><mml:mrow><mml:mtext>K</mml:mtext></mml:mrow></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-175"><mml:math id="mml-ieqn-175"><mml:mi>g</mml:mi></mml:math></inline-formula></term>
<def>
<p>Acceleration due to gravity <inline-formula id="ieqn-176"><mml:math id="mml-ieqn-176"><mml:msup><mml:mrow><mml:mtext>s</mml:mtext></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-177"><mml:math id="mml-ieqn-177"><mml:mi>h</mml:mi></mml:math></inline-formula></term>
<def>
<p>Heat transfer coefficient <inline-formula id="ieqn-178"><mml:math id="mml-ieqn-178"><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mtext>W</mml:mtext></mml:mrow><mml:mrow><mml:msup><mml:mrow><mml:mtext>m</mml:mtext></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mrow><mml:mtext>K</mml:mtext></mml:mrow></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-179"><mml:math id="mml-ieqn-179"><mml:msub><mml:mi>h</mml:mi><mml:mrow><mml:mi>a</mml:mi></mml:mrow></mml:msub></mml:math></inline-formula></term>
<def>
<p>Coefficient of heat transfer at temperature <inline-formula id="ieqn-180"><mml:math id="mml-ieqn-180"><mml:msub><mml:mrow><mml:mtext>T</mml:mtext></mml:mrow><mml:mrow><mml:mrow><mml:mtext>a</mml:mtext></mml:mrow></mml:mrow></mml:msub></mml:math></inline-formula> <inline-formula id="ieqn-181"><mml:math id="mml-ieqn-181"><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mtext>W</mml:mtext></mml:mrow><mml:mrow><mml:msup><mml:mrow><mml:mtext>m</mml:mtext></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mrow><mml:mtext>K</mml:mtext></mml:mrow></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-182"><mml:math id="mml-ieqn-182"><mml:msub><mml:mi>i</mml:mi><mml:mrow><mml:mi>f</mml:mi><mml:mi>g</mml:mi></mml:mrow></mml:msub></mml:math></inline-formula></term>
<def>
<p>Latent heat of water evaporation <inline-formula id="ieqn-183"><mml:math id="mml-ieqn-183"><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mtext>J</mml:mtext></mml:mrow><mml:mrow><mml:mtext>kg</mml:mtext></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-184"><mml:math id="mml-ieqn-184"><mml:mi>k</mml:mi></mml:math></inline-formula></term>
<def>
<p>Thermal conductivity <inline-formula id="ieqn-185"><mml:math id="mml-ieqn-185"><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mtext>W</mml:mtext></mml:mrow><mml:mrow><mml:mtext>mK</mml:mtext></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-186"><mml:math id="mml-ieqn-186"><mml:mi>K</mml:mi></mml:math></inline-formula></term>
<def>
<p>Permeability <inline-formula id="ieqn-187"><mml:math id="mml-ieqn-187"><mml:msup><mml:mrow><mml:mtext>m</mml:mtext></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-188"><mml:math id="mml-ieqn-188"><mml:mi>L</mml:mi></mml:math></inline-formula></term>
<def>
<p>Length of the fin <inline-formula id="ieqn-189"><mml:math id="mml-ieqn-189"><mml:mrow><mml:mtext>m</mml:mtext></mml:mrow></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-190"><mml:math id="mml-ieqn-190"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>0</mml:mn></mml:mrow></mml:msub><mml:mo>,</mml:mo><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>1</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula></term>
<def>
<p>Constants <inline-formula id="ieqn-191"><mml:math id="mml-ieqn-191"><mml:mo>&#x2212;</mml:mo></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-192"><mml:math id="mml-ieqn-192"><mml:msub><mml:mi>m</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math></inline-formula></term>
<def>
<p>Wet porous parameter <inline-formula id="ieqn-193"><mml:math id="mml-ieqn-193"><mml:mo>&#x2212;</mml:mo></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-194"><mml:math id="mml-ieqn-194"><mml:mi>N</mml:mi><mml:mi>c</mml:mi></mml:math></inline-formula></term>
<def>
<p>Convection parameter <inline-formula id="ieqn-195"><mml:math id="mml-ieqn-195"><mml:mo>&#x2212;</mml:mo></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-196"><mml:math id="mml-ieqn-196"><mml:mi>N</mml:mi><mml:mi>r</mml:mi></mml:math></inline-formula></term>
<def>
<p>Radiative parameter <inline-formula id="ieqn-197"><mml:math id="mml-ieqn-197"><mml:mo>&#x2212;</mml:mo></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-198"><mml:math id="mml-ieqn-198"><mml:mi>S</mml:mi><mml:mi>h</mml:mi></mml:math></inline-formula></term>
<def>
<p>Porosity parameter <inline-formula id="ieqn-199"><mml:math id="mml-ieqn-199"><mml:mo>&#x2212;</mml:mo></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-200"><mml:math id="mml-ieqn-200"><mml:msub><mml:mi>t</mml:mi><mml:mrow><mml:mi>b</mml:mi></mml:mrow></mml:msub></mml:math></inline-formula></term>
<def>
<p>Base thickness of the fin <inline-formula id="ieqn-201"><mml:math id="mml-ieqn-201"><mml:mrow><mml:mtext>m</mml:mtext></mml:mrow></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-202"><mml:math id="mml-ieqn-202"><mml:mi>T</mml:mi></mml:math></inline-formula></term>
<def>
<p>Fluid temperature <inline-formula id="ieqn-203"><mml:math id="mml-ieqn-203"><mml:mrow><mml:mtext>K</mml:mtext></mml:mrow></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-204"><mml:math id="mml-ieqn-204"><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi>a</mml:mi></mml:mrow></mml:msub></mml:math></inline-formula></term>
<def>
<p>Ambient temperature <inline-formula id="ieqn-205"><mml:math id="mml-ieqn-205"><mml:mrow><mml:mtext>K</mml:mtext></mml:mrow></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-206"><mml:math id="mml-ieqn-206"><mml:msub><mml:mi>T</mml:mi><mml:mrow><mml:mi>b</mml:mi></mml:mrow></mml:msub></mml:math></inline-formula></term>
<def>
<p>Base temperature<inline-formula id="ieqn-207"><mml:math id="mml-ieqn-207"><mml:mrow><mml:mtext>K</mml:mtext></mml:mrow></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-208"><mml:math id="mml-ieqn-208"><mml:msup><mml:mi>t</mml:mi><mml:mrow><mml:mo>&#x2217;</mml:mo></mml:mrow></mml:msup></mml:math></inline-formula></term>
<def>
<p>Semi fin thickness <inline-formula id="ieqn-209"><mml:math id="mml-ieqn-209"><mml:mrow><mml:mtext>m</mml:mtext></mml:mrow></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-210"><mml:math id="mml-ieqn-210"><mml:mi>x</mml:mi></mml:math></inline-formula></term>
<def>
<p>Fin length <inline-formula id="ieqn-211"><mml:math id="mml-ieqn-211"><mml:mrow><mml:mtext>m</mml:mtext></mml:mrow></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-212"><mml:math id="mml-ieqn-212"><mml:mi>X</mml:mi></mml:math></inline-formula></term>
<def>
<p>Non-dimensional axial co-ordinate <inline-formula id="ieqn-213"><mml:math id="mml-ieqn-213"><mml:mo>&#x2212;</mml:mo></mml:math></inline-formula></p>
</def>
</def-item>
</def-list>
<def-list>
<title>Greek Symbols
</title>
<def-item>
<term><inline-formula id="ieqn-214"><mml:math id="mml-ieqn-214"><mml:mi>&#x03B8;</mml:mi></mml:math></inline-formula></term>
<def>
<p>Non-dimensional temperature <inline-formula id="ieqn-215"><mml:math id="mml-ieqn-215"><mml:mo>&#x2212;</mml:mo></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-216"><mml:math id="mml-ieqn-216"><mml:mi>&#x03C3;</mml:mi></mml:math></inline-formula></term>
<def>
<p>Stefan-Boltzmann constant <inline-formula id="ieqn-217"><mml:math id="mml-ieqn-217"><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mtext>W</mml:mtext></mml:mrow><mml:mrow><mml:msup><mml:mrow><mml:mtext>m</mml:mtext></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:msup><mml:mrow><mml:mtext>K</mml:mtext></mml:mrow><mml:mrow><mml:mn>4</mml:mn></mml:mrow></mml:msup></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-218"><mml:math id="mml-ieqn-218"><mml:mi>&#x03B5;</mml:mi></mml:math></inline-formula></term>
<def>
<p>Surface emissivity of fin</p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-219"><mml:math id="mml-ieqn-219"><mml:mi>&#x03C1;</mml:mi></mml:math></inline-formula></term>
<def>
<p>Density <inline-formula id="ieqn-220"><mml:math id="mml-ieqn-220"><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mtext>kg</mml:mtext></mml:mrow><mml:msup><mml:mrow><mml:mtext>m</mml:mtext></mml:mrow><mml:mrow><mml:mn>3</mml:mn></mml:mrow></mml:msup></mml:mfrac></mml:mstyle></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-221"><mml:math id="mml-ieqn-221"><mml:mi>&#x03BC;</mml:mi></mml:math></inline-formula></term>
<def>
<p>Dynamic viscosity <inline-formula id="ieqn-222"><mml:math id="mml-ieqn-222"><mml:mstyle displaystyle="true" scriptlevel="0"><mml:mfrac><mml:mrow><mml:mtext>kg</mml:mtext></mml:mrow><mml:mrow><mml:mrow><mml:mtext>m</mml:mtext></mml:mrow><mml:mo>.</mml:mo><mml:mrow><mml:mtext>s</mml:mtext></mml:mrow></mml:mrow></mml:mfrac></mml:mstyle></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-223"><mml:math id="mml-ieqn-223"><mml:mi>&#x03D5;</mml:mi></mml:math></inline-formula></term>
<def>
<p>Nanoparticle volume fraction parameter <inline-formula id="ieqn-224"><mml:math id="mml-ieqn-224"><mml:mo>&#x2212;</mml:mo></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-225"><mml:math id="mml-ieqn-225"><mml:mi>&#x03C4;</mml:mi></mml:math></inline-formula></term>
<def>
<p>Angle of inclination <inline-formula id="ieqn-226"><mml:math id="mml-ieqn-226"><mml:mo>&#x2212;</mml:mo></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-227"><mml:math id="mml-ieqn-227"><mml:mtext>&#x0393;</mml:mtext></mml:math></inline-formula></term>
<def>
<p>Time constant <inline-formula id="ieqn-228"><mml:math id="mml-ieqn-228"><mml:mo>&#x2212;</mml:mo></mml:math></inline-formula></p>
</def>
</def-item>
</def-list>
<def-list>
<title>Subscript
</title>
<def-item>
<term><inline-formula id="ieqn-229"><mml:math id="mml-ieqn-229"><mml:mi>f</mml:mi></mml:math></inline-formula></term>
<def>
<p>Base fluid <inline-formula id="ieqn-230"><mml:math id="mml-ieqn-230"><mml:mo>&#x2212;</mml:mo></mml:math></inline-formula></p>
</def>
</def-item>
<def-item>
<term><inline-formula id="ieqn-231"><mml:math id="mml-ieqn-231"><mml:mi>h</mml:mi><mml:mi>n</mml:mi><mml:mi>f</mml:mi></mml:math></inline-formula></term>
<def>
<p>Hybrid nanofluid <inline-formula id="ieqn-232"><mml:math id="mml-ieqn-232"><mml:mo>&#x2212;</mml:mo></mml:math></inline-formula></p>
</def>
</def-item>
</def-list>
</glossary>
<ref-list content-type="authoryear">
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