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1-13 of 13
Yann G. Guezennec
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Proceedings Papers
Proc. ASME. FUELCELL2010, ASME 2010 8th International Fuel Cell Science, Engineering and Technology Conference: Volume 1, 581-592, June 14–16, 2010
Paper No: FuelCell2010-33171
Abstract
Proton Exchange Membrane Fuel Cell performance significantly depends on electrode water content. Indeed, an excess of liquid water in the pores of the gas diffusion layer (GDL) and in the gas flow channel (GFC) can drastically bring down the output power. Depending on the operating conditions, liquid water emerging from the GDL micro-channels can form droplets, films or slugs in the GFC. In the regime of droplets formation, the interaction with the gas crossing-flow leads to an oscillating mechanisms that is fundamental to studying the detachment from the GDL surface, as the authors have shown in a previous publication. In this work, a numerical model of a droplet growing on the GDL surface is developed to describe the interaction between droplet cross-flowing gas stream. The droplet shape and its deformation are reconstructed assuming a known geometry. Therefore, a lumped force balance is enforced to determine the center of mass motion law. Oscillation frequencies during growth and at detachment are found as a function of droplet size. The model is also exploited to find the relationship between droplet critical detachment size and gas velocity. The numerical results are compared with the droplet frequency-size and detachment size-gas velocity experimental results previously presented by the authors. The matching between the numerical and experimental data is very good and is a mean of validation for the model. The low computational burden and the conciseness of the results make the model suitable for applications such as control and optimization strategies development to enhance PEMFC performance. Additionally, the model can be exploited to implement monitoring and diagnostic algorithm.
Journal Articles
Article Type: Research Papers
J. Electrochem. En. Conv. Stor. June 2010, 7(3): 031021.
Published Online: March 17, 2010
Abstract
An accurate low order model (mean value model) that captures main water transport mechanisms through the components of a PEM fuel cell was developed. Fast simulation time was achieved through a lumped approach in modeling the space-dependent phenomena. Evaporation and capillarity were assumed to be the predominant mechanisms of water flow through the gas diffusion media. The innovative features of the model are not only to simulate the water transport inside the porous media with relative simplicity, but also to simulate the water transport at the interface between the gas diffusion layer and gas flow channel. In order to preserve a light computational burden, the complex air flow-droplet interaction was modeled with several simplifying assumptions, and with the support of measured data. The physics that characterizes the single droplet-air flow interaction was analyzed with an experimental apparatus constructed to study the droplet growth and detachment process. Furthermore, the experimental findings were exploited to feed the numerical model with the missing theoretical information, and empirical submodels to guarantee accuracy. Thanks to the followed fast computational time of the mean value approach, the model is suitable for fuel cell design and optimization, as well as diagnosis and control strategies development studies.
Proceedings Papers
Proc. ASME. FUELCELL2009, ASME 2009 7th International Conference on Fuel Cell Science, Engineering and Technology, 411-420, June 8–10, 2009
Paper No: FuelCell2009-85166
Abstract
An accurate low order model (MVM, Mean Value Model) that captures the main water transport mechanisms through the components of a PEM Fuel Cell was developed. Fast simulation time was achieved through a lumped approach in modeling space-dependent phenomena. Evaporation and capillarity were assumed to be the predominant mechanisms of water flow through the gas diffusion media. The model innovative features are not only to simulate the water transport inside the porous media with relative simplicity but also to simulate the water transport at the interface between gas diffusion layer and gas flow channel. In order to preserve a light computational burden, the complex air flow–droplets interaction was modeled with several simplifying assumption and with the support of measured data. The physics that characterizes the single droplet-air flow interaction was analyzed with an experimental apparatus constructed to study the droplet growth and detachment process. Furthermore, the experimental findings were exploited to feed the numerical model with the missing theoretical information and empirical sub-models to guarantee accuracy. Thanks to the fast computational time of the mean value approach followed, the model is suitable for fuel cell design and optimization as well as diagnosis and control strategies development studies.
Proceedings Papers
Proc. ASME. IMECE2008, Volume 8: Energy Systems: Analysis, Thermodynamics and Sustainability; Sustainable Products and Processes, 407-416, October 31–November 6, 2008
Paper No: IMECE2008-68742
Abstract
In this work, an accurate and computationally fast model for liquid water transport within a proton exchange membrane fuel cell (PEMFC) electrode is developed by lumping the space-dependence of the relevant variables. Capillarity is considered as the main transport mechanism within the gas diffusion layer (GDL). The novelty of the model lies in the simulation of the water transport at the interface between gas diffusion layer and gas flow channel (GFC). This is achieved with a phenomenological description of the process that allows its simulation with relative simplicity. Moreover, a detailed two-dimensional visualization of such interface is achieved via geometric simulation of water droplets formation, growth, coalescence and detachment on the surface of the GDL. The accomplishment of reduced computational time and good accuracy makes the model suitable for control strategy implementation to ensure PEM fuel cells operation within optimal electrode water content. Furthermore, the model is useful for optimization analysis oriented to both PEMFC design and balance of plant.
Proceedings Papers
Proc. ASME. ICES2002, Design, Operation, and Application of Modern Internal Combustion Engines and Associated Systems, 179-186, April 14–17, 2002
Paper No: ICES2002-463
Abstract
A novel fuel atomization device (Nanomiser™) was evaluated under laboratory conditions with respect to its ability to reduce SI engine cold-start hydrocarbon emissions. First, comparisons between the level of atomization using the conventional, pintle-type fuel injector and the novel atomizer were carried out using flow visualization in a spray chamber and particle size distribution. The novel atomizer is capable of producing sub-micron fuel droplets, which form an ultra-fine mist with outstanding non-wetting characteristics. To capitalize on these atomization characteristics, this device was compared to a conventional fuel injector in a small, two-cylinder, SI engine under a number of operating conditions. Results show a slightly enhanced combustion quality and lean limit under warm operating conditions and a dramatic reduction in unburned HC emission under cold operating conditions, with cold emissions with the Nanomiser™ matching those with a conventional injector under fully warm conditions.
Proceedings Papers
Proc. ASME. FUELCELL2006, ASME 2006 Fourth International Conference on Fuel Cell Science, Engineering and Technology, Parts A and B, 411-422, June 19–21, 2006
Paper No: FUELCELL2006-97237
Abstract
Dynamic behavior and transient analysis are one of the most critical issues for high performance polymeric electrolyte membrane fuel cells. An improvement of performance can be achieved both with hardware modifications and with more sophisticated control strategies. To this regard, the availability of a reliable dynamic fuel cell model plays an important role in the design of fuel cell control and diagnostic system. This paper presents a non-linear, iso-thermal, zero-dimensional model of a pressurized PEM fuel cell system used for automotive applications. The model was derived from a detailed, iso-thermal, steady-state, dimensional model which explicitly calculated (and subsequently captured as a multi-D look-up table) the relationship between cathode and anode pressures and humidity and stack average current. Since in the electrochemical model the single cell performance depends on the membrane ionic resistance, which is strictly related to the membrane water content, a dynamic estimation of the membrane water diffusion has been considered. This takes into account the dependence of the cell voltage on the unsteady membrane water concentration. A similar approach still allows the development of a simple zero-dimensional dynamic model suitable for control system development and amenable to control-oriented humidity modelling.
Proceedings Papers
Marco Sorrentino, Ashraf Mandourah, Thomas F. Petersen, Yann G. Guezennec, Michael J. Moran, Giorgio Rizzoni
Proc. ASME. IMECE2004, Advanced Energy Systems, 205-214, November 13–19, 2004
Paper No: IMECE2004-60927
Abstract
A one-dimensional steady-state model for planar solid oxide fuel cells (SOFCs) is presented. Appropriately simplified, the model includes sufficient detail for supporting ongoing investigations involving the simulation of SOFC-based advanced energy systems. The presentation focuses on a set of nonlinear equations accounting for conservation of mass and energy along a single SOFC in a co-flow configuration. Electrochemical models also are employed, including one previously used for a zero dimensional approach. The equations are described through a phenomenological approach based on the best recent work in the field and model validation is carried out in two distinct phases using previously published information. Potential areas of application for the model presented are noted.
Proceedings Papers
Proc. ASME. IMECE2005, Dynamic Systems and Control, Parts A and B, 1265-1272, November 5–11, 2005
Paper No: IMECE2005-82359
Abstract
This paper deals with the development of a control-oriented model for simulation of planar solid oxide fuel cells (SOFCs). A hierarchical modeling structure has been set-up to identify a simplified model that allows describing the dynamic behavior of an SOFC with satisfactory accuracy, affordable computational burden and limited amount of experimental data. Particularly in this work, a steady-state relationship that links cell voltage to current density and temperature has been inferred from a phenomenological 1-D model previously developed by the authors. Then, a first order model has been obtained by applying the conservation of energy principle (heat balance) to a lumped control volume that includes air and fuel channels, interconnect and solid tri-layer ( i.e. , electrolyte and electrodes). A state-space representation of the model also is presented, having the cell outlet temperature and the cell voltage as state and output variables, respectively. Model validation has been conducted by comparing the cell response to load ( i.e. , current density) variations with data generated by means of a physical comprehensive model previously published by Achenbach. Extensive simulation of the cell dynamic behavior has been performed in order to analyze the main system dynamics with respect to changes in cell temperature, load, excess air and fuel utilization. The results of this analysis will serve as a tool for both optimal design and sizing, as well as for the energy management of hybridized ( i.e. supported by batteries or supercap) SOFC-based power generation systems.
Proceedings Papers
Proc. ASME. IMECE2006, Dynamic Systems and Control, Parts A and B, 343-349, November 5–10, 2006
Paper No: IMECE2006-14608
Abstract
During a battery's lifetime, its performance slowly deteriorates because of the degradation of its electrochemical constituents. This degradation produces undesirable effects that include the loss of rated capacity, faster temperature rise during operation, less charge acceptance, higher internal resistance, lower voltage, and more frequent self-discharge. The most drastic effect is the loss of capacity. This paper presents a method to quantify the electrochemical process behind the aging of a battery by using electrochemical impedance spectroscopy as a tool to measure the change in battery parameters. While classical methods would relate battery age to impedance measurements at one specific frequency, this method measures the battery impedance at different frequencies and evaluates the variation in the frequency response spectrum with respect to battery age. The variation of the impedance spectrum from one experiment to another allows to get a better characterization of the aging process.
Proceedings Papers
Proc. ASME. IMECE2006, Dynamic Systems and Control, Parts A and B, 493-504, November 5–10, 2006
Paper No: IMECE2006-15338
Abstract
Due to sharply increasing oil price, tremendous efforts are being made to reduce the dependencies on the petroleum based fuels in the field of automotive power trains. As one of the promising alternatives, fuel cell hybrid system has been studied for many different vehicle types from SUV to low speed vehicle. To establish systematic ways to achieve the optimized system configuration, in this paper, we introduce a methodology which combines energy analysis over typical drive cycles with a parametric sizing study for the various powertrain components as well as supervisory energy management parameters. For a practical and demonstrative implementation of the suggested methodology with a limited resource available at hand, a Neighborhood Electric Vehicle (NEV) for urban transportation is considered for a detailed analysis, design and optimization. Two major supervisory control strategies, namely, charge-sustaining and charge-depleting are carefully investigated to illustrate the versatility of our proposed methodology. Our study shows that the systems could be modeled and optimized either in a charge sustaining case or in a charge depleting case (plug-in hybrid electric vehicle) to meet vehicle purposes and usages, respectively. Not only because of the usage of the FC power system as a range extender for an EV, but also the possibility of using the plug-in configuration with renewable energy generation systems, as a personal eco-system, the proposed plug-in FC-NEV may be a solution for a local urban transportation system in this demanding era of sustainable mobility.
Journal Articles
Daisie D. Boettner, Mem. ASME, Gino Paganelli, Yann G. Guezennec, Mem. ASME, Giorgio Rizzoni, Mem. ASME, Michael J. Moran, Mem. ASME, Fellow ASME
Article Type: Technical Papers
J. Energy Resour. Technol. September 2002, 124(3): 191–196.
Published Online: August 6, 2002
Abstract
This paper incorporates a methanol reformer model with a proton exchange membrane (PEM) fuel cell system model for automotive applications. The reformer model and fuel cell system model have been integrated into a vehicle performance simulator that determines fuel economy and other performance features. Fuel cell vehicle fuel economy using on-board methanol reforming is compared with fuel economy using direct-hydrogen fueling. The overall performance using reforming is significantly less than in a direct-hydrogen fuel cell vehicle.
Journal Articles
Daisie D. Boettner, Mem. ASME, Gino Paganelli, Mem. ASME, Yann G. Guezennec, Mem. ASME, Giorgio Rizzoni, Mem. ASME, Michael J. Moran, Fellow ASME, Mem. ASME
Article Type: Technical Papers
J. Energy Resour. Technol. March 2002, 124(1): 20–27.
Published Online: March 25, 2002
Abstract
This paper describes a proton exchange membrane (PEM) fuel cell system model for automotive applications that includes an air compressor, cooling system, and other auxiliaries. The fuel cell system model has been integrated into a vehicle performance simulator that determines fuel economy and allows consideration of control strategies. Significant fuel cell system efficiency improvements may be possible through control of the air compressor and other auxiliaries. Fuel cell system efficiency results are presented for two limiting air compressor cases: ideal control and no control. Extension of the present analysis to hybrid configurations consisting of a fuel cell system and battery is currently under study.
Journal Articles
Article Type: Technical Papers
J. Eng. Gas Turbines Power. July 2000, 122(3): 493–501.
Published Online: October 21, 1999
Abstract
The work described in this paper focuses on experiments to quantify the initial fuel mixing and gross fuel distribution in the cylinder during the intake stroke and its relationship to the large-scale convective flow field. The experiments were carried out in a water analog engine simulation rig, and, hence, limited to the intake stroke. The same engine head configuration was used for the three-dimensional PTV flow field and the PLIF fuel concentration measurements. High-speed CCD cameras were used to record the time evolution of the dye convection and mixing with a 1/4 deg of crank angle resolution (and were also used for the three-dimensional PTV measurements). The captured sequences of images were digitally processed to correct for background light non-uniformity and other spurious effects. The results are finely resolved evolution of the dye concentration maps in the center tumble plane. The three-dimensional PTV measurements show that the flow is characterized by a strong tumble, as well as pairs of cross-tumble, counter-rotating eddies. The results clearly show the advection of a fuel-rich zone along the wall opposite to the intake valves and later along the piston crown. It also shows that strong out-of-plane motions further contribute to the cross-stream mixing to result in a relatively uniform concentration at BDC, albeit slightly stratified by the lean fluid entering the cylinder later in the intake stroke. In addition to obtaining phase-averaged concentration maps at various crank angles throughout the intake stroke, the same data set is processed for a large number of cycle to extract spatial statistics of the cycle-to-cycle variability and spatial non-uniformity of the concentration maps. The combination of the three-dimensional PTV and PLIF measurements provides a very detailed understanding of the advective mixing properties of the intake-generated flow field. [S0742-4795(00)00103-4]