Planar Multiplexing of Microfluidic Fuel Cells

2013 ◽  
Vol 135 (2) ◽  
Author(s):  
Bernard Ho ◽  
Erik Kjeang

Microfluidic fuel cells eliminate the membrane by utilizing parallel colaminar flow of electrolyte between the anode and cathode electrodes. When operated on vanadium redox electrolyte, these cells also eliminate the need for catalyst. Hence, microfluidic fuel cells are promising contenders in terms of achieving useful performance levels for commercial applications while being cost-effective on a commercial scale. However, due to the inherent size of these devices the power output is relatively low and scale-up is a major challenge. In the present article, two planar cell multiplexing strategies are introduced, featuring a nonsymmetric unilateral design and a symmetric bilateral device architecture, both of which employ two cells with shared fluidic inlet ports. The fuel cell design is based on flow-through porous carbon electrodes using vanadium redox electrolytes as reactants. In both array architectures, the two cells are fluidically connected in parallel and electrically in series. The main challenge of achieving uniform flow distribution is assessed using laminar flow theory and computational fluid dynamics and validated experimentally. The normalized performance obtained with the two prototype array cells is found to be equivalent to previously reported data for single cells, in this case doubling the device level voltage and power output and reaching 820 and 1200 mW/cm2 peak power density for the nonsymmetric unilateral and symmetric bilateral array designs, respectively. It is, thus, demonstrated that both unilateral and bilateral planar multiplexing strategies are feasible for microfluidic fuel cell technologies and are shown to be particularly effective when the flow sharing between different cells is equal.

2006 ◽  
Vol 3 (3) ◽  
pp. 226-233 ◽  
Author(s):  
Andrea Baratella ◽  
Roberto Bove ◽  
Piero Lunghi

Testing the performance of fuel cells is an important key for verifying technology improvements and for demonstrating their potential. However, due to the novelty of this technology, there is not a standardized procedure for testing fuel cell performance. In order to fully investigate fuel cell performance, the behavior must be known under a wide range of operational conditions. Furthermore, in order to compare results coming from different test teams, a set of procedures and parameters to evaluate single cell performance should be defined. The research group of the Fuel Cell Laboratory of the University of Perugia is conducting performance tests on single cells, focusing on defining test procedures to find effective parameters to be used to compare tests performed by different teams. This work demonstrates how the testing parameters developed by the team allow one to perform advanced control on test procedures, to understand test results, and to compare them with tests carried out under different operational conditions. The entire analysis is easily conducted by using a single parameter variation hyperspace approach. The experimental results obtained on single fuel cells are reported.


Author(s):  
Shuo-Jen Lee ◽  
Kung-Ting Yang ◽  
Yu-Ming Lee ◽  
Chi-Yuan Lee

In this research, electrochemical impedance spectroscopy is employed to monitor the resistance of a fuel cell during operation with different operating conditions and different materials for the bipolar plates. The operating condition variables are cell humidity, pure oxygen or air as oxidizer, and current density. Three groups of single cells were tested: a graphite cell, a stainless steel cell (treated and original), and a thin, small, treated stainless steel cell. A treated cell here means using an electrochemical treatment to improve bipolar plate anticorrosion capability. From the results, the ohmic resistance of a fully humidified treated stainless steel fuel cell is 0.28 Ω cm2. Under the same operating conditions, the ohmic resistance of the graphite and the original fuel cell are each 0.1 Ω cm2 and that of the small treated cell is 0.3 Ω cm2. Cell humidity has a greater influence on resistance than does the choice of oxidizer; furthermore, resistance variation due to humidity effects is more serious with air support. From the above results, fuel cells fundamental phenomenon such as ohmic resistance, charge transfer resistance, and mass transport resistance under different operating conditions could be evaluated.


Author(s):  
Piero Lunghi ◽  
Gianni Bidini

Fuel cells are known to be efficient and environmental friendly electricity generation devices. Great expectations are put on their contribution for future ultra-clean energy production. Nevertheless, the requests from deregulated energy market prompt fast commercialization of systems that are not yet fully optimized. Low efficiencies of first generation commercial fuel cell plants could result in failure when satisfying end users’ requirements thus creating an obstacle for subsequent market penetration. In this context, the availability of reliable data on fuel cells, necessary for their correct integration in full energy systems for plant optimization and feasibility assessment constitutes a priority. On the other hand, while measuring fuel cells performance is a difficult task nevertheless within reach for most research departments; the challenge for the scientific community is to reliably assess performance dependence on all the most relevant input parameters. As a result, most of the experimental data find on literature on fuel cells performances refer to voltage measures at increasing currents for fixed gas compositions and flow rates. In this work an experimental facility has been set up, test rigs have been designed and constructed both for fuel cells and reforming section testing; the main aim was to allow great operational flexibility. Great attention has been paid on test procedures and on input parameterisation as well on reliable advanced control systems. Dependence on the most relevant input parameters, i.e. current density, operating temperature, fuel and oxidant utilization factor, fuel humidification and dilution has been deeply analysed. Performances have been analysed both in terms of output voltage and efficiency and in terms of time degradation and expected total lifetime. The contribution of the work done consist in defining adimensional parameters which, thanks to their direct relation with the theoretical equations which govern a fuel cell, can greatly improve performance evaluation capability of experimental tests. Moreover those parameters can represent a way to standardize test procedures and constitute a means for comparing and exchanging results in a easier and effective way. A second contribution consist in designing and developing a unique control system that can improve test reliability thanks to the feature that allows to change single parameters while keeping the others constant and greatly enhance the number of experimental points that can be obtained in a test.


Author(s):  
Peiwen Li ◽  
Devasubramaniam Coopamah ◽  
Jeong-Pill Ki

This paper presents the results obtained from the study about flow distribution in maintaining uniformity of flow fields in fuel cells. Three novel flow distribution designs on bipolar plates are proposed for a proton exchange membrane fuel cell (PEMFC). The flow distributors have multiple levels of bifurcations to split a flow into sub-streams of equal flow rates. There are three types of bifurcation structure proposed and studied, which are the 90° tee-type, rounded-type and slanted-type. Experiments were carried out to test the velocities of flows from the multiple channels after bifurcations, and the flow uniformity on the bipolar plate is estimated and studied. Overall evaluation of flow uniformity in the three designs was conducted. The rounded-type bifurcation structure showed the best flow uniformity. After experimental verification of the uniform flow distribution in the novel design, three PEM fuel cell was fabricated which adopted the novel flow fields. From the experimental test and comparison under dry fuel and air condition, it is found that the PEMFC with new flow field can have a better performance. Thorough experimental investigation is planned for the future study.


RSC Advances ◽  
2017 ◽  
Vol 7 (57) ◽  
pp. 35613-35618 ◽  
Author(s):  
Joyotu Mazumder ◽  
Hiroyuki Yoshikawa ◽  
Hideo Miyake ◽  
Toshiyuki Shibata ◽  
Eiichi Tamiya

An alginate fuel cell comprising a TiO2-modified carbon sheet (TiO2/C) anode was developed. The power output of the fuel cell and decomposition of alginate were enhanced by solar irradiation of the anode.


Author(s):  
P. W. Li ◽  
S. P. Chen ◽  
M. K. Chyu

In order to improve the power output of a fuel cell, a novel approach for gas delivery and mass transfer enhancement in a gas distributor is proposed. A model analyzing the power output against the dimensions of a novel gas delivery channel and current collector is also presented. Experimental study for some proton-exchange-membrane fuel cells and numerical analysis for a planar type solid oxide fuel cell are carried out. Significant improvement of power output was obtained for the newly designed fuel cells compared to conventional ones. Both the experimental results and modeling analysis are of great significance to the design of fuel cells.


Author(s):  
Robert Radu ◽  
Nicola Zuliani ◽  
Rodolfo Taccani

Proton exchange membrane (PEM) fuel cells based on polybenzimidazole (PBI) polymers and phosphoric acid can be operated at temperature between 120 °C and 180 °C. Reactant humidification is not required and CO content up to 1% in the fuel can be tolerated, only marginally affecting performance. This is what makes high-temperature PEM (HTPEM) fuel cells very attractive, as low quality reformed hydrogen can be used and water management problems are avoided. From an experimental point of view, the major research effort up to now was dedicated to the development and study of high-temperature membranes, especially to development of acid-doped PBI type membranes. Some studies were dedicated to the experimental analysis of single cells and only very few to the development and characterization of high-temperature stacks. This work aims to provide more experimental data regarding high-temperature fuel cell stacks, operated with hydrogen but also with different types of reformates. The main design features and the performance curves obtained with a three-cell air-cooled stack are presented. The stack was tested on a broad temperature range, between 120 and 180 °C, with pure hydrogen and gas mixtures containing up to 2% of CO, simulating the output of a typical methanol reformer. With pure hydrogen, at 180 °C, the considered stack is able to deliver electrical power of 31 W at 1.8 V. With a mixture containing 2% of carbon monoxide, in the same conditions, the performance drops to 24 W. The tests demonstrated that the performance loss caused by operation with reformates, can be partially compensated by a higher stack temperature.


2011 ◽  
Vol 17 (2) ◽  
pp. 207-214 ◽  
Author(s):  
T. Selyari ◽  
A.A. Ghoreyshi ◽  
M. Shakeri ◽  
G.D. Najafpour ◽  
T. Jafary

In this study, a single polymer electrolyte membrane fuel cell (PEMFC) in H2/O2 form with an effective dimension of 5?5 cm as well as a single direct methanol fuel cell (DMFC) with a dimension of 10?10 cm were fabricated. In an existing test station, the voltage-current density performances of the fabricated PEMFC and DMFC were examined under various operating conditions. As was expected DMFC showed a lower electrical performance which can be attributed to the slower methanol oxidation rate in comparison to the hydrogen oxidation. The results obtained from the cell operation indicated that the temperature has a great effect on the cell performance. At 60?C, the best power output was obtained for PEMFC. There was a drop in the cell voltage beyond 60?C which can be attributed to the reduction of water content inside the membrane. For DMFC, maximum power output was resulted at 64oC. Increasing oxygen stoichiometry and total cell pressure had a marginal effect on the cell performance. The results also revealed that the cell performance improved by increasing pressure differences between anode and cathode. A unified semi-empirical thermodynamic based model was developed to describe the cell voltage as a function of current density for both kinds of fuel cells. The model equation parameters were obtained through a nonlinear fit to the experimental data. There was a good agreement between the experimental data and the model predicted cell performance for both types of fuel cells.


Processes ◽  
2021 ◽  
Vol 9 (6) ◽  
pp. 985
Author(s):  
Wei Han Tan ◽  
Siewhui Chong ◽  
Hsu-Wei Fang ◽  
Kuan-Lun Pan ◽  
Mardawani Mohamad ◽  
...  

Microbial fuel cell (MFC) technology has attracted a great amount of attention due to its potential for organic and inorganic waste treatment concomitant with power generation. It is thus seen as a clean energy alternative. Modifications and innovations have been conducted on standalone and hybrid/coupled MFC systems to improve the power output to meet the end goal, namely, commercialization and implementation into existing wastewater treatment plants. As the energy generated is inversely proportional to the size of the reactor, the stacking method has been proven to boost the power output from MFC. In recent years, stacked or scale-up MFCs have also been used as a power source to provide off-grid energy, as well as for in situ assessments. These scale-up studies, however, encountered various challenges, such as cell voltage reversal. This review paper explores recent scale-up studies, identifies trends and challenges, and provides a framework for current and future research.


2020 ◽  
Vol 5 (8) ◽  
pp. 822-827
Author(s):  
Govindarasu Ramasamy ◽  
R. Kavitha ◽  
M. Nambiraj ◽  
R. Praveen Kumaar ◽  
N. N. Harish Kumar

Fuel cells are the devices that convert chemical energy into electrical energy through an electrochemical reaction. Direct Methanol Fuel cell (DMFC) is a proton exchange membrane fuel cells in which methanol is used as fuel. Its high energy density makes it suitable for fuel cells. Even though carbon dioxide is produced, there is no production of sulfur or nitrogen oxides. The problems usually occurred while working with DMFC are methanol crossover, condensation of methanol, water management and carbon dioxide release. In that the uneven flow distribution, accumulation of carbon dioxide bubbles in the fuel cell are the major issues in DMFC. To prevent these issues, this work focuses on the theoretical and experimental studies on development of fuel cells with special importance to geometry of the manifold. This paper provides the optimal solution for preventing uneven flow distribution that is the usage of squoval shaped manifold which is the combination of both square and circle. Performance of DMFC with squoval shape manifold is evaluated experimentally and is compared with square shape manifold and rectangle shape manifold geometry design.


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