This study investigates the various uses of density of motile microorganisms in the context of the flow of a binary base fluid with double diffusion past a vertical surface. The research aims to comprehend the interactions between motile microorganisms and the fluid dynamics, as well as the heat and mass transport mechanisms in this system. The analysis involves mathematically constructing the governing equations, transforming them into dimensionless nonlinear ordinary differential equations using similarity transformations, and numerically solving them using the MATLAB bvp4c solver. An analysis of the influence of several parameters on the profiles of velocity, temperature, concentration, nanoparticle concentration, and density of motile microorganisms is conducted using graphical representation. The findings demonstrate that boosting the thermophoresis parameter intensifies the temperature profile. In addition, an increase in the nanofluid Schmidt number results in a larger concentration of nanoparticles, whereas a higher bioconvection Lewis number reduces the density of the motile microorganism profile. These findings may find use in biomedical engineering as well as industrial processes that include enhancing the efficiency of mass transfer and bioconvection. Numeric simulation prophesies 99.9% for both shear stress and heat transfer rate intensification for Prandtl values are noticed.
{"title":"A multiple applications study of motile microorganisms past a vertical surface with double-diffusive binary base fluid","authors":"Battina Madhusudhana Rao, Putta Durgaprasad, Gurram Dharmaiah, Saeed Dinarvand, Saurav Gupta","doi":"10.1002/htj.23142","DOIUrl":"https://doi.org/10.1002/htj.23142","url":null,"abstract":"<p>This study investigates the various uses of density of motile microorganisms in the context of the flow of a binary base fluid with double diffusion past a vertical surface. The research aims to comprehend the interactions between motile microorganisms and the fluid dynamics, as well as the heat and mass transport mechanisms in this system. The analysis involves mathematically constructing the governing equations, transforming them into dimensionless nonlinear ordinary differential equations using similarity transformations, and numerically solving them using the MATLAB bvp4c solver. An analysis of the influence of several parameters on the profiles of velocity, temperature, concentration, nanoparticle concentration, and density of motile microorganisms is conducted using graphical representation. The findings demonstrate that boosting the thermophoresis parameter intensifies the temperature profile. In addition, an increase in the nanofluid Schmidt number results in a larger concentration of nanoparticles, whereas a higher bioconvection Lewis number reduces the density of the motile microorganism profile. These findings may find use in biomedical engineering as well as industrial processes that include enhancing the efficiency of mass transfer and bioconvection. Numeric simulation prophesies 99.9% for both shear stress and heat transfer rate intensification for Prandtl values are noticed.</p>","PeriodicalId":44939,"journal":{"name":"Heat Transfer","volume":"53 8","pages":"4468-4487"},"PeriodicalIF":2.8,"publicationDate":"2024-08-07","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142587946","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Maham Mujahid, Zaheer Abbas, Muhammad Yousuf Rafiq
Pressure-driven movement is a fundamental concept with numerous applications in various industries, scientific disciplines, and fields of engineering. Its proper execution is vital for promoting revolutionary innovations and providing solutions in numerous sectors. Therefore, this article scrutinizes the pressure-driven flow of magnetized Casson fluid between two curved corrugated walls. The geometry of the channel is represented mathematically in an orthogonal curvilinear coordinate system. The corrugation grooves are described by sinusoidal functions with phase differences between the corrugated curved walls. The boundary perturbation method is used to find the analytical solution for the velocity field and volumetric flow rate, taking the corrugation amplitude as the perturbation parameter. The results show that the peak of the velocity increases with the radius of curvature and the width of the channel for a constant pressure gradient. The velocity exhibited a declining trend due to an increase in the Casson fluid parameter. For a sufficiently large corrugation wavenumber, the flow rate decreases, and the phase difference becomes irrelevant. However, the reduction in flow can be minimized by decreasing the channel radius of curvature. In general, a smooth curved channel will give the maximum flow rate for a large corrugation wavenumber. The model can be used to simulate blood flow in arteries with varying geometries and magnetic fields, aiding in the study of cardiovascular diseases and the design of medical devices like stents.
{"title":"A study on the pressure-driven flow of magnetized non-Newtonian Casson fluid between two corrugated curved walls of an arbitrary phase difference","authors":"Maham Mujahid, Zaheer Abbas, Muhammad Yousuf Rafiq","doi":"10.1002/htj.23146","DOIUrl":"https://doi.org/10.1002/htj.23146","url":null,"abstract":"<p>Pressure-driven movement is a fundamental concept with numerous applications in various industries, scientific disciplines, and fields of engineering. Its proper execution is vital for promoting revolutionary innovations and providing solutions in numerous sectors. Therefore, this article scrutinizes the pressure-driven flow of magnetized Casson fluid between two curved corrugated walls. The geometry of the channel is represented mathematically in an orthogonal curvilinear coordinate system. The corrugation grooves are described by sinusoidal functions with phase differences between the corrugated curved walls. The boundary perturbation method is used to find the analytical solution for the velocity field and volumetric flow rate, taking the corrugation amplitude as the perturbation parameter. The results show that the peak of the velocity increases with the radius of curvature and the width of the channel for a constant pressure gradient. The velocity exhibited a declining trend due to an increase in the Casson fluid parameter. For a sufficiently large corrugation wavenumber, the flow rate decreases, and the phase difference becomes irrelevant. However, the reduction in flow can be minimized by decreasing the channel radius of curvature. In general, a smooth curved channel will give the maximum flow rate for a large corrugation wavenumber. The model can be used to simulate blood flow in arteries with varying geometries and magnetic fields, aiding in the study of cardiovascular diseases and the design of medical devices like stents.</p>","PeriodicalId":44939,"journal":{"name":"Heat Transfer","volume":"53 8","pages":"4510-4527"},"PeriodicalIF":2.8,"publicationDate":"2024-08-07","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142587948","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Md. Nasim Mia, Muhammad Abdullah, Arpita Das, Fahim Tanfeez Mahmood, Mohammad Nasim Hasan
The current study presents a computational investigation of mixed convective heat transfer in a square enclosure containing power-law fluid. An active flow modulator is employed in the form of a flat plate with negligible thickness, and the mixed convection is achieved through clockwise rotation of the plate. The rotation of the plate is modeled by incorporating a moving mesh technique. The solution is then obtained by applying the Finite Element Technique under the arbitrary Lagrangian–Eulerian framework. Numerical validation is performed with contemporary research studies consisting of rotating plates to justify the accuracy of the present study. The study is conducted at constant Prandtl number Pr = 1.0 and Reynolds number Re = 500 while varying the power-law index (0.6 ≤ n ≤ 1.4) and the Richardson number (0.1 ≤ Ri ≤ 10.0). The results have been presented in terms of the flow and thermal fields, spatially averaged Nusselt number, spatially averaged power consumption by the plate, and the velocity and temperature profile in the enclosure. The numerical findings indicate that a higher Richardson number encourages heat transfer. For the shear-thinning fluid, a 37% thermal augmentation is observed in comparison to the Newtonian fluid at Ri = 10. However, in the case of shear-thickening fluid, thermal performance was reduced by 21.13%. Small thermal oscillations are observed in naturally dominated mixed convection for shear-thinning fluids, but none are observed for shear-thickening or Newtonian fluids. In addition, the findings demonstrate that the flow modulator has a positive impact on heat transfer for the shear-thickening fluids (n > 1) and an adverse effect for the shear-thinning fluids (n < 1). Furthermore, the power consumption decreases as Ri increases, and it becomes negative beyond Ri = 1.0 due to the increase in natural convection strength.
本研究对含有幂律流体的方形外壳中的混合对流传热进行了计算研究。采用的主动流动调节器是厚度可忽略不计的平板,通过顺时针旋转平板实现混合对流。平板的旋转是通过移动网格技术模拟的。然后在任意拉格朗日-欧拉框架下应用有限元技术求解。为了证明本研究的准确性,我们利用由旋转板组成的当代研究成果进行了数值验证。研究在普朗特数 Pr = 1.0 和雷诺数 Re = 500 不变的条件下进行,同时改变幂律指数(0.6 ≤ n ≤ 1.4)和理查德森数(0.1 ≤ Ri ≤ 10.0)。结果显示了流场和热场、空间平均努塞尔特数、板的空间平均功率消耗以及围护结构中的速度和温度分布。数值结果表明,理查德森数越大,热量传递越快。对于剪切稀化流体,与 Ri = 10 时的牛顿流体相比,热量增加了 37%。然而,在剪切增稠流体的情况下,热性能降低了 21.13%。在剪切稀化流体的自然主导混合对流中观察到了微小的热振荡,但在剪切增稠流体或牛顿流体中均未观察到。此外,研究结果表明,流动调节器对剪切增稠流体(n >1)的热传递有积极影响,而对剪切稀化流体(n <1)则有不利影响。此外,由于自然对流强度的增加,功耗随着 Ri 的增加而降低,超过 Ri = 1.0 时,功耗变为负值。
{"title":"Mixed convective heat transfer in a square cavity filled with power-law fluids under active flow modulation","authors":"Md. Nasim Mia, Muhammad Abdullah, Arpita Das, Fahim Tanfeez Mahmood, Mohammad Nasim Hasan","doi":"10.1002/htj.23143","DOIUrl":"https://doi.org/10.1002/htj.23143","url":null,"abstract":"<p>The current study presents a computational investigation of mixed convective heat transfer in a square enclosure containing power-law fluid. An active flow modulator is employed in the form of a flat plate with negligible thickness, and the mixed convection is achieved through clockwise rotation of the plate. The rotation of the plate is modeled by incorporating a moving mesh technique. The solution is then obtained by applying the Finite Element Technique under the arbitrary Lagrangian–Eulerian framework. Numerical validation is performed with contemporary research studies consisting of rotating plates to justify the accuracy of the present study. The study is conducted at constant Prandtl number <i>Pr</i> = 1.0 and Reynolds number <i>Re</i> = 500 while varying the power-law index (0.6 ≤ <i>n</i> ≤ 1.4) and the Richardson number (0.1 ≤ <i>Ri</i> ≤ 10.0). The results have been presented in terms of the flow and thermal fields, spatially averaged Nusselt number, spatially averaged power consumption by the plate, and the velocity and temperature profile in the enclosure. The numerical findings indicate that a higher Richardson number encourages heat transfer. For the shear-thinning fluid, a 37% thermal augmentation is observed in comparison to the Newtonian fluid at <i>Ri</i> = 10. However, in the case of shear-thickening fluid, thermal performance was reduced by 21.13%. Small thermal oscillations are observed in naturally dominated mixed convection for shear-thinning fluids, but none are observed for shear-thickening or Newtonian fluids. In addition, the findings demonstrate that the flow modulator has a positive impact on heat transfer for the shear-thickening fluids (<i>n</i> > 1) and an adverse effect for the shear-thinning fluids (<i>n</i> < 1). Furthermore, the power consumption decreases as <i>Ri</i> increases, and it becomes negative beyond <i>Ri</i> = 1.0 due to the increase in natural convection strength.</p>","PeriodicalId":44939,"journal":{"name":"Heat Transfer","volume":"53 8","pages":"4422-4447"},"PeriodicalIF":2.8,"publicationDate":"2024-08-06","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142588099","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Heat exchangers are crucial in transferring heat and finding applications across various industries. Numerous strategies have been devised to improve and optimize the heat transfer process within these systems. Among these, passive methods have garnered significant attention for their ability to operate without external power consumption. This article examines the recent experimental and computational studies conducted by researchers since 2018 on passive enhancement techniques, especially twisted tape, wire coil, swirl flow generator, and others, to boost the thermal efficiency of heat exchangers and aid designers in adopting passive augmentation methods for compact heat exchangers. Recently, researchers' new class of flow maldistribution devices, referred to as swirl flow devices, has gained attention; which enhances convective heat transfer by introducing swirl into the main flow and disrupting the boundary layer at the tube surface through alterations in surface geometry. Twisted tape inserts are devices that demonstrate better performance in laminar flow compared to turbulent flow. Conversely, other passive techniques like ribs, conical nozzles, and conical rings are generally more effective in turbulent flow than laminar flow. A recent research trend is the utilization of nanofluids in combination with other passive heat transfer enhancement techniques like turbulators, ribs, and twisted tape inserts in heat exchangers, which can reduce exergy losses and improve overall convective heat transfer coefficient and effectiveness of heat exchanger.
{"title":"Enhancing heat exchanger performance with perforated/non-perforated flow modulators generating continuous/discontinuous swirl flow: A comprehensive review","authors":"Md Atiqur Rahman, S. M. Mozammil Hasnain","doi":"10.1002/htj.23135","DOIUrl":"https://doi.org/10.1002/htj.23135","url":null,"abstract":"<p>Heat exchangers are crucial in transferring heat and finding applications across various industries. Numerous strategies have been devised to improve and optimize the heat transfer process within these systems. Among these, passive methods have garnered significant attention for their ability to operate without external power consumption. This article examines the recent experimental and computational studies conducted by researchers since 2018 on passive enhancement techniques, especially twisted tape, wire coil, swirl flow generator, and others, to boost the thermal efficiency of heat exchangers and aid designers in adopting passive augmentation methods for compact heat exchangers. Recently, researchers' new class of flow maldistribution devices, referred to as swirl flow devices, has gained attention; which enhances convective heat transfer by introducing swirl into the main flow and disrupting the boundary layer at the tube surface through alterations in surface geometry. Twisted tape inserts are devices that demonstrate better performance in laminar flow compared to turbulent flow. Conversely, other passive techniques like ribs, conical nozzles, and conical rings are generally more effective in turbulent flow than laminar flow. A recent research trend is the utilization of nanofluids in combination with other passive heat transfer enhancement techniques like turbulators, ribs, and twisted tape inserts in heat exchangers, which can reduce exergy losses and improve overall convective heat transfer coefficient and effectiveness of heat exchanger.</p>","PeriodicalId":44939,"journal":{"name":"Heat Transfer","volume":"53 8","pages":"4364-4393"},"PeriodicalIF":2.8,"publicationDate":"2024-08-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142588202","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
This work provides an analytical and numerical assessment, complete with correlations, of mixed convection in a double lid-driven shallow rectangular enclosure, which confines non-Newtonian fluids of the Ostwald–de Waele type and which a uniform thermal flux heats. The finite volume method with the SIMPLER algorithm is the numerical method used to solve the governing partial differential equations along with the boundary conditions, where the parallel flow concept is the analytical approach. In the limits of the explored values of the governing parameters of this study, which are the Rayleigh number, the Peclet number, and the behavior index, the results obtained by these approaches appear to be in good harmony. On the basis of the results obtained by these approaches, we established helpful correlating relations between the governing parameters to realize the contribution of mixed convection to heat transfer. This leads to the finding that the ratio Ra/Pe2+n is the mixed convection parameter, which is the key to distinguishing the three convective flow modes. On the basis of this parameter, which allows the transition from one regime to another, it is possible to identify the zones that designate the predominance of natural, forced, and mixed convection. The limits of these latter depend on the behavior index, n, which is diversified from 0.6 to 1.4 to account for shear thinning (0 < n < 1, low apparent viscosity, high fluid flow, and high heat transfer rate), Newtonian (n = 1), and shear thickening (n > 1, high apparent viscosity, slow fluid flow, and low heat transfer rate) fluids. On the other hand, the study presents and interprets the influences of the steering factors on heat transfer and fluid flow.
{"title":"Correlations of mixed convection in a double lid-driven shallow rectangular cavity: The case of non-Newtonian power-law fluids","authors":"A. Louaraychi, M. Lamsaadi","doi":"10.1002/htj.23138","DOIUrl":"https://doi.org/10.1002/htj.23138","url":null,"abstract":"<p>This work provides an analytical and numerical assessment, complete with correlations, of mixed convection in a double lid-driven shallow rectangular enclosure, which confines non-Newtonian fluids of the Ostwald–de Waele type and which a uniform thermal flux heats. The finite volume method with the SIMPLER algorithm is the numerical method used to solve the governing partial differential equations along with the boundary conditions, where the parallel flow concept is the analytical approach. In the limits of the explored values of the governing parameters of this study, which are the Rayleigh number, the Peclet number, and the behavior index, the results obtained by these approaches appear to be in good harmony. On the basis of the results obtained by these approaches, we established helpful correlating relations between the governing parameters to realize the contribution of mixed convection to heat transfer. This leads to the finding that the ratio <i>Ra</i>/<i>Pe</i><sup>2+</sup><sup><i>n</i></sup> is the mixed convection parameter, which is the key to distinguishing the three convective flow modes. On the basis of this parameter, which allows the transition from one regime to another, it is possible to identify the zones that designate the predominance of natural, forced, and mixed convection. The limits of these latter depend on the behavior index, <i>n</i>, which is diversified from 0.6 to 1.4 to account for shear thinning (0 < <i>n</i> < 1, low apparent viscosity, high fluid flow, and high heat transfer rate), Newtonian (<i>n</i> = 1), and shear thickening (<i>n</i> > 1, high apparent viscosity, slow fluid flow, and low heat transfer rate) fluids. On the other hand, the study presents and interprets the influences of the steering factors on heat transfer and fluid flow.</p>","PeriodicalId":44939,"journal":{"name":"Heat Transfer","volume":"53 8","pages":"4394-4421"},"PeriodicalIF":2.8,"publicationDate":"2024-08-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142588205","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
The heat transfer in power-law fluids across three corrugated circular cylinders placed in a triangular pitch arrangement is studied computationally in a confined channel. Continuity, momentum, and energy balance equations were solved using ANSYS FLUENT (Version 18.0). The flow is assumed to be steady, incompressible, two-dimensional, and laminar. A square domain of side 300Dh is selected after a detailed domain study. An optimized grid with 98,187 cells is used in the study. The convergence criteria of 10−7 for the continuity, x-momentum, and y-momentum balances and 10−12 for the energy equation were used. Constant density and non-Newtonian power-law viscosity modules were used. The diffusive term is discretized using a central difference scheme. Convective terms are discretized using the Second-Order Upwind scheme. Pressure–velocity coupling between continuity and momentum equations was implemented using the semi-implicit method for pressure-linked equation scheme. Streamlines show wake development behind the cylinders, which is very dominant at large ReN and n. Isotherm contours are cramped at higher values of ReN and PrN, implying higher heat transfer. Global parameters, like, Cd and Nu, are computed for the wide ranges of controlling dimensionless parameters, such as power-law index (0.3 ≤ n ≤ 1.5), Reynolds (0.1 ≤ ReN ≤ 40), and Prandtl (0.72 ≤ PrN ≤ 500) numbers. The NuLocal plot attains a pitch near the corrugation of the surface due to abrupt changes in velocity and temperature gradients. Nu increases with ReN and/or PrN and decreases with n under ot herwise identical situations. Nu is correlated with pertinent parameters, namely, ReN, PrN, and n.
{"title":"CFD study of heat transfer in power-law fluids over multiple corrugated circular cylinders in a heat exchanger","authors":"Sonam Gopaldasji Rajpuriya, Radhe Shyam","doi":"10.1002/htj.23133","DOIUrl":"https://doi.org/10.1002/htj.23133","url":null,"abstract":"<p>The heat transfer in power-law fluids across three corrugated circular cylinders placed in a triangular pitch arrangement is studied computationally in a confined channel. Continuity, momentum, and energy balance equations were solved using ANSYS FLUENT (Version 18.0). The flow is assumed to be steady, incompressible, two-dimensional, and laminar. A square domain of side 300<i>D</i><sub><i>h</i></sub> is selected after a detailed domain study. An optimized grid with 98,187 cells is used in the study. The convergence criteria of 10<sup>−7</sup> for the continuity, <i>x</i>-momentum, and <i>y</i>-momentum balances and 10<sup>−12</sup> for the energy equation were used. Constant density and non-Newtonian power-law viscosity modules were used. The diffusive term is discretized using a central difference scheme. Convective terms are discretized using the Second-Order Upwind scheme. Pressure–velocity coupling between continuity and momentum equations was implemented using the semi-implicit method for pressure-linked equation scheme. Streamlines show wake development behind the cylinders, which is very dominant at large <i>Re</i><sub><i>N</i></sub> and <i>n</i>. Isotherm contours are cramped at higher values of <i>Re</i><sub><i>N</i></sub> and <i>Pr</i><sub><i>N</i></sub>, implying higher heat transfer. Global parameters, like, <i>C</i><sub><i>d</i></sub> and <i>Nu</i>, are computed for the wide ranges of controlling dimensionless parameters, such as power-law index (0.3 ≤ <i>n</i> ≤ 1.5), Reynolds (0.1 ≤ <i>Re</i><sub><i>N</i></sub> ≤ 40), and Prandtl (0.72 ≤ <i>Pr</i><sub><i>N</i></sub> ≤ 500) numbers. The <i>Nu</i><sub><i>Local</i></sub> plot attains a pitch near the corrugation of the surface due to abrupt changes in velocity and temperature gradients. <i>Nu</i> increases with <i>Re</i><sub><i>N</i></sub> and/or <i>Pr</i><sub><i>N</i></sub> and decreases with <i>n</i> under ot herwise identical situations. <i>Nu</i> is correlated with pertinent parameters, namely, <i>Re</i><sub><i>N</i></sub>, <i>Pr</i><sub><i>N</i></sub>, and <i>n</i>.</p>","PeriodicalId":44939,"journal":{"name":"Heat Transfer","volume":"53 8","pages":"4339-4363"},"PeriodicalIF":2.8,"publicationDate":"2024-07-30","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142588236","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Previous works that investigated the characteristics of heat transfer and fluid flow in channels with corrugated walls have been extensively reviewed in this study. In accordance with the fast increase in power consumption requirements, many researchers have investigated a new approach for cooling techniques that can enhance the cooling performance of devices without consuming more power. To improve the efficiency of energy systems, many investigators and engineers implement promising techniques such as surface optimization and additives as passive methods to augment the rates of heat transfer. Researchers investigated different corrugation profiles along with various working fluids as well as external power devices to further improve the heat exchange process of thermal systems. The aim of this article is to give a clear preview of the effects of different parameters such as wave parameters, Reynolds number, type of working fluid, and pulsating flow condition on the average and local Nusselt number, the pressure drop, the performance factors, and irreversibility. The main findings are listed in tables and depicted in figures, the matter that helps engineers and researchers to choose a suitable channel shape for their applications.
{"title":"Characteristics of thermo-hydraulic flow inside corrugated channels: Comprehensive and comparative review","authors":"Fatimah Q. AL-Daamee, Naseer H. Hamza","doi":"10.1002/htj.23136","DOIUrl":"10.1002/htj.23136","url":null,"abstract":"<p>Previous works that investigated the characteristics of heat transfer and fluid flow in channels with corrugated walls have been extensively reviewed in this study. In accordance with the fast increase in power consumption requirements, many researchers have investigated a new approach for cooling techniques that can enhance the cooling performance of devices without consuming more power. To improve the efficiency of energy systems, many investigators and engineers implement promising techniques such as surface optimization and additives as passive methods to augment the rates of heat transfer. Researchers investigated different corrugation profiles along with various working fluids as well as external power devices to further improve the heat exchange process of thermal systems. The aim of this article is to give a clear preview of the effects of different parameters such as wave parameters, Reynolds number, type of working fluid, and pulsating flow condition on the average and local Nusselt number, the pressure drop, the performance factors, and irreversibility. The main findings are listed in tables and depicted in figures, the matter that helps engineers and researchers to choose a suitable channel shape for their applications.</p>","PeriodicalId":44939,"journal":{"name":"Heat Transfer","volume":"53 8","pages":"4285-4315"},"PeriodicalIF":2.8,"publicationDate":"2024-07-26","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"141800297","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Nitul Kalita, Himangshu Kumar, Rupam Shankar Nath, Rudra Kanta Deka
<p>The purpose of this study is to analyze how thermal stratification affects fluid movement past an impulsively initiated infinite upright plate when first-order chemical reactions are present. Laplace's transform method is applied to achieve a closed-form solution for the nondimensional governing equations when <span></span><math>