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جستجوی مقالات مرتبط با کلیدواژه « fuel cell performance » در نشریات گروه « فنی و مهندسی »

  • عبدالکریم افروزه*

    نانوتکنولوژی در توسعه و بهبود عملکرد پیل های سوختی اکسید جامد (SOFC) به خوبی استفاده می شود. دمای عملیاتی بالای SOFC (700-900 درجه سلسیوس) منجر به نواقصی جدی در ارتباط با عملکرد کلی و دوام آنها شده است. از این رو، دمای عملیاتی بالا به دامنه دمای متوسط تقریبا 44-700 سلسیوس کاهش یافته است که عملکرد را بهبود بخشیده است و متعاقبا SOFC را به عنوان منابع انرژی قابل حمل تجاری کرده است. با این حال، در دمای کاهش یافته، چالش هایی مانند افزایش مقاومت داخلی اجزای پیل سوختی بوجود می آیند. اگر چه، این مساله نمی تواند به اندازه مشکلاتی که در دمای بالا بوجود می آید، جدی باشد، هنوز به شکل قابل توجهی بر عملکرد SOFC تاثیر می گذارد. این مقاله به کار محققان در زمینه کاربرد نانوتکنولوژی در ساخت SOFC از طریق روش های متمایز می پردازد. این روش ها با موفقیت مقاومت داخلی را حذف یا حداقل کاهش داده اند و بهبود قابل توجه در تراکم انرژی SOFC در دماهای کاهش یافته را نشان داده اند.

    کلید واژگان: پیل سوختی اکسید جامد, توسعه مواد, نانوماده ها, عملکرد پیل سوختی}
    Abdolkarim Afroozeh*

    Nanotechnology is well used in the development and performance improvement of solid oxide fuel cells (SOFCs). The high operating temperature of SOFCs (700-900 ° C) has led to serious shortcomings in their overall performance and durability. Hence, the high operating temperature has been reduced to the average temperature range of approximately 44-700 Celsius, which has improved performance and subsequently commercialized SOFCs as portable energy sources. However, at reduced temperatures, challenges arise such as increasing the internal strength of fuel cell components. Although this may not be as serious as the problems that arise at high temperatures, it still significantly affects SOFC performance. This paper deals with the work of researchers in the field of application of nanotechnology in the construction of SOFC through different methods. These methods have successfully eliminated or minimized internal resistance and shown significant improvements in SOFC energy density at reduced temperatures.

    Keywords: Solid oxide fuel cell, material development, nanomaterials, fuel cell performance}
  • N. Ahmadi, H. Taraghi, M. Sadeghiazad
    Modeling the heat and mass transport in micro channel is being used extensively in researches and industrial applications. The aim is optimizing fuel cell designs before building a prototype for engineering application. In this study, numerical, three-dimensional, single phase computational fluid dynamics model of a proton exchange membrane fuel cell with both the gas distribution flow channels and the Membrane Electrode Assembly (MEA) has been developed. A single set of conservation equations which are valid for the flow channels, gas-diffusion electrodes, catalyst layers, and the membrane region, are solved by finite volume technique. The present simulated straight channels PEMFC model, accounts for major transport phenomena and the performance. Additionally, the effect of reversing the flow direction at cathode side has been investigated to study the fuel cell performance and species distribution. The results showed that, in the PEMFC with the counter flow channels, the output current density has been decreased and also the kind of species distributions has been influenced by this phenomenon. It is very important to model the back diffusion and electro-osmotic mass flux for determination of ionic conductivity of membrane which affects the performance of fuel cell. Finally, the numerical results are validated by available experimental data.
    Keywords: PEM fuel cells, cell voltage, current density, counter flow, fuel cell performance}
  • S. A. Rezazadeh, I. Mirzaie, N. Pourmahmoud, N. Ahmadi
    A full three-dimensional, single phase computational fluid dynamics model of a proton exchange membrane fuel cell (PEMFC) with both the gas distribution flow channels and the Membrane Electrode Assembly (MEA) has been developed. A single set of conservation equations which are valid for the flow channels, gas-diffusion electrodes, catalyst layers, and the membrane region are developed and numerically solved using a finite volume based computational fluid dynamics technique. In this research some parameters such as oxygen consumption, water production, temperature distribution, ohmic losses, anode water activity, cathode over potential and the fuel cell performance for straight single cell were investigated in more details. The numerical simulations reveal that these important operating parameters are highly dependent to each other and the fuel cell efficiency is affected by the kind of species distribution. So for especial uses in desirable voltages, for preventing from the unwilling losses, these numerical results can be useful. Finally the numerical results of proposed CFD model have been compared with the published experimental data that represent good agreement.
    Keywords: PEM fuel cell, Ohmic loss, water activity, CFD, Fuel cell performance}
  • A. Torkavannejad, S. Mehdi Pesteei, I. Mirzaee, F. Ramin
    computational fluid dynamics analysis was employed to investigate the species distribution of proton exchange membrane fuel cells (PEMFC) with different channel geometries at high operating current densities. 3D, non-isothermal was used with single straight channel geometry. Our study showed that an elliptical and circular channel cross-section gave higher current density compared with conventional model. However, the elliptical and circular channel configuration facilitated reactant transportation, cause to more homogenous reactants distribution and thus to a lower cathode overpotential of the cell which is the main losses is regard to it. Simulation of the three different channel revealed shoulder width has dominating effect on cells performance and lead to increase the value of Ohmic loss. The numerical model is validated against published experimental data with good agreement. Other result with more detail are discussed and presented in the text.
    Keywords: channel cross, section, Fuel cell performance, PEM fuel cells, Single, phase}
  • A. Torkavannejad*, M. Pesteei, M. Khalilian, F. Ramin, I. Mirzaee
    This article presents the results of a numerical study, using computational fluid dynamics (CFD) analysis to investigate the species distribution of proton exchange membrane fuel cells (PEMFCs) with deflected membrane electrode assembly (MEA). These new geometry were examined while employing three-dimensional, single phase, non-isothermal and parallel flow for model of a PEM fuel cell. This numerical research has concentrated on the effect of new kind of deflected MEA while maintaining the same inlet and boundary condition. Initially, the CFD result of polarization curve has been validated with the available experimental data and shown good concord; then, studied deflected and flatted MEA at cathode and anode side. Investigation showed better results for the PEMFC with having both flatted and deflected MEA at cathode side than base model because of having more reacting area, uniform distribution of reactants, better oxygen transportation to the GDL at shoulder region and having less Cathode Overpotential (COP) which is the main causes of losses.
    Keywords: Deflection, Fuel Cell Performance, PEM Fuel Cells, Single, Phase}
  • باقر کاظمی نسب*، سوسن روشن ضمیر، حسین قدمیان
    لایه کاتالیست اغلب نازک ترین لایه در پیل سوختی است، اما به خاطر چند فازی، تخلخل و واکنش های الکتروشیمیایی پیچیده ترین قسمت است. عملکرد پیل سوختی غشا تبادل پروتون شدیدا متاثر از عملکرد لایه کاتالیست کاتد است. در این تحقیق یک مدل یک بعدی، دما ثابت و پایا با ساختار کلوخه ای برای لایه کاتالیست کاتد در نظر گرفته شده و توسعه یافته است. پس از نوشتن معادلات حاکم لایه کاتالیست، معادلات دیفرانسیلی برای متغیرهای مستقل دانسیته جریان، غلظت اکسیژن و افت فعال سازی حاصل شده که به همراه شرایط مرزی مربوطه یک دستگاه معادلات دیفرانسیل معمولی مرتبه اول غیرخطی را تشکیل می دهند. دستگاه معادلات با کد نویسی در نرم افزار Matlab نسخه 2011، به وسیله روش پرتابی و توابع مساله مقدار مرزی حل شده است. پس از اعتبار سنجی مدل با نتایج تئوری و تجربی، مطالعه پارامتری جامعی از اثر چهارده پارامتر شامل پارامترهای عملیاتی دما، فشار و اشباع آب و پارامترهای ساختاری لایه کاتالیست مانند مقدار پلاتین، جز حجمی یونومر، تخلخل و ضخامت لایه کاتالیست، شعاع و تخلخل کلوخه و غیره بر عملکرد پیل سوختی انجام شده است. مشخص شد که پارامترهای اشباع آب، شعاع کلوخه و جز حجمی یونومر بیشترین تاثیر را بر عملکرد لایه کاتالیست دارند.
    کلید واژگان: پیل سوختی غشا تبادل پروتون, مدل کلوخه ای, عملکرد پیل سوختی, مدل سازی لایه کاتالیست کاتد, مطالعه پارامتری جامع}
    Bagher Kazeminasab *, Soosan Rowshanzamir, Hossein Ghadamian
    The catalyst layer is often the thinnest layer in the fuel cell، but is often the most complex part due to multiple phases، porosity، and electrochemical reactions. The performance of proton exchange membrane (PEM) fuel cell is strongly affected by the cathode catalyst layer performance. In this study، a steady state isothermal one-dimensional agglomerate model is considered and developed for the cathode catalyst layer. After writing the governing equations for the catalyst layer، differential equations for independent variables of current density، oxygen concentration and activation overpotential obtained that form a coupled system of first-order nonlinear ordinary differential equations (ODE’s) with the related boundary conditions. Then coupled system of ODE’s is solved through coding in Matlab software version 2011، using a shooting method، boundary value problem (BPV). After validating the model against experimental and theoretical results، a comprehensive parametric study is performed on the effects of fourteen parameters including operational parameters namely temperature، pressure and saturation liquid water، and structural parameters such as platinum loading، ionomer volume fraction، porosity and thickness of catalyst layer، radius and porosity of agglomerate and etc. on the catalyst layer performance. It was found that saturation liquid water، ionomer volume fraction and agglomerate radius have the greatest effect on the performance.
    Keywords: PEM Fuel Cell, Agglomerate Model, Fuel cell Performance, Cathode Catalyst Layer Modeling, Comprehensive Parametric Study}
  • Ashkan Torkavannejad, Farzin Ramin, Sima Baheri
    Computational fluid dynamics analysis was employed to investigate the radial flow field patterns of proton exchange membrane fuel cells (PEMFC) with different channel geometries at high operating current densities. 3D, non-isothermal was used with single straight channel geometry. Our study showed that new generation of fuel cells with circle stack with the same active area and inlet area gave higher current density compared with conventional model. the main factors that affect the behavior of each of the curves are discussed. Species and temperature contours are presented for the new model, showing how the fuel cell behavior is affected by species penetration due to increasing inlet and outlet in one mono cell (four inlet and out let) with inclined in the radial channel configuration.Velocity trends are presented for the two different models, showing how the fuel cell behavior is affected by the velocity variations in the radial configuration. Thus, the results presented here suggest that the radial geometry is a strong candidate for the near-future development of the fuel cell technology.
    Keywords: Fuel cell performance, PEM fuel cells, Single, phase, Radial channel flow}
  • سیدعلی اطیابی، ابراهیم افشاری، محمود عدمی
    در این مطالعه، با قرار دادن یک یا چند مانع در کانال کاتد پیل سوختی غشا پلیمری، تاثیرات دینامیک سیالات ناشی از وجود/عدم وجود مانع در کانال و همچنین اثر مانع بر عملکرد پیل سوختی مورد مطالعه قرار گرفته است. بدین منظور با در نظر گرفتن یک مدل سه بعدی پیل سوختی که بخشی از کانال کاتد مسدود شده است، معادلات پیوستگی، مومنتوم، گونه های جرمی و بقای بار الکتریکی به صورت حالت پایا در سیستم مختصات کارتزین با استفاده از یک دامنه کلی و روش حجم محدود حل شده است. نتایج نشان می دهد که با قرار دادن یک مانع، در مقایسه با حالت بدون مانع، بیشترین افزایش سرعت در لایه پخش گاز (زیر مانع حدود 6 برابر سرعت) رخ داده است و گازهای واکنش دهنده بیشتری مجبور به ورود به لایه پخش گاز می شود که به واکنش های شیمیایی کمک می کند و عملکرد پیل سوختی را بهبود می بخشد. همچنین افزایش تعداد موانع بر انتقال گازهای واکنش دهنده و توزیع یکنواخت تر گازها در لایه پخش گاز و لایه کاتالیست، مخصوصا در دانسیته جریان های بالا، کمک می کند؛ اما افت فشار در کانال کاتد را افزایش می دهد. پیش بینی ها نشان می دهد که انتقال موضعی واکنش دهنده، تولید چگالی جریان محلی و عملکرد پیل در حضور موانع بهبود می یابد.
    کلید واژگان: پیل سوختی غشا پلیمری, مانع, انتقال اکسیژن, افت فشار, عملکرد پیل سوختی}
    Seyed Ali Atyabi, Ebrahim Afshari, Mahmood Adami
    In this study، we propose a configuration of partially blocked oxidant channel with baffle plates transversely inserted in the cathode channel and effects of the fluid dynamics due to the presence or non-presence of the baffles and their effect on the fuel cell performance is investigated. A 3D model with the presence of baffle plates is considered and a set of equations (continuity، momentum، species and charge together with electrochemical kinetics) in the form of single domain is developed and solved numerically. The baffles block the main flow in the cathode channel and force more reactant gases to turn to the GDL. This fact implies an enhancement of the oxygen flux at the GDL and catalyst surface، especially at the position beneath the location of the baffle plates. An increase in the number of baffles contribute to the reactant gas transport to GDL with more uniform distribution of gas in the GDL and catalyst layer، specially in high current densities، where it leads to a penalty of high pressure – loss. The predictions indicate that the local transport of the reactant gas would enhance the local current densities and the fuel cell performance in presence of baffle in the channel.
    Keywords: PEMFC, Baffle, Oxygen transport, Pressure drop, Fuel cell performance}
  • N.Ahmadi, N.Pourmahmoud, I.Mirzaee, S.Rezazadeh
    A full three-dimensional, single phase computational fluid dynamics model of a proton exchange membrane fuel cell (PEMFC) with both the gas distribution flow channels and the Membrane Electrode Assembly (MEA) has been developed. A single set of conservation equations which are valid for the flow channels, gas-diffusion electrodes, catalyst layers, and the membrane region are developed and numerically solved using a finite volume based computational fluid dynamics technique. In this research, some important parameters such as variation of oxygen and water mass fraction, liquid water activity and the membrane protonic conductivity have been presented at the entry and exit regions of the cell. The numerical results indicated that, at lower cell voltage (0.6v) which corresponds to higher current density, the hydrogen and oxygen consumption and, accordingly water production is high. Finally the numerical results of the proposed CFD model are compared with the available experimental data that represent good agreement.
    Keywords: PEM fuel cells, cell potential, current density, CFD, fuel cell performance}
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