Development of Production Technology for Membrane-Electrode Assemblies With Radical Capturing Layer

2013 ◽  
Vol 10 (1) ◽  
Author(s):  
Toshiro Kobayashi ◽  
Etsuro Hirai ◽  
Hideki Itou ◽  
Takuya Moriga

This paper describes the development of mass-production technology for membrane-electrode assemblies (MEA) with a radical capturing layer and verifies its performance. Some of the authors of this paper previously developed an MEA with a radical capturing layer along the boundaries between the electrode catalyst layer and the polymer membrane to realize an endurance time of 20,000 h in accelerated daily start and daily stop (DSS) deterioration tests. Commercialization of these MEAs requires a production technology that suits mass production lines and provides reasonable cost performance. After developing a water-based slurry and selecting a gas diffusion layer (GDL), a catalyst layer forming technology uses a rotary screen method for electrode formation. Studies confirmed continuous formation of the catalyst layer, obtaining an anode/cathode thickness of 55 μm (+10/−20)/50 μm (+10/−20) by optimizing the opening ratio and thickness of the screen plate. A layer-forming technology developed for the radical capturing layer uses a two-fluid spraying method. Continuous formation of an 8 μm thick (±3 μm) radical capturing layer proved feasible by determining the appropriate slurry viscosity, spray head selection, and optimization of spraying conditions.

Author(s):  
T. Kobayashi ◽  
E. Hirai ◽  
H. Itoh ◽  
T. Moriga

This paper describes the development of mass-production technology for membrane-electrode assemblies (MEA) with a radical capturing layer and verifies its performance. Some of the authors of this paper previously developed an MEA with a radical capturing layer along the boundaries between the electrode catalyst layer and the polymer membrane to realize an endurance time of 20,000 h in accelerated daily start and daily stop (DSS) deterioration tests. Commercialization of these MEAs requires a production technology that suits mass production lines and provides reasonable cost performance. After developing a water-based slurry and selecting a gas diffusion layer (GDL), a catalyst layer forming technology uses a rotary screen method for electrode formation. Studies confirmed continuous formation of the catalyst layer, obtaining an anode/cathode thickness of 55 μm (+10/−20)/50 μm (+10/−20) by optimizing the opening ratio and thickness of the screen plate. A layer-forming technology developed for the radical capturing layer uses a two-fluid spraying method. Continuous formation of an 8-μm-thick (±3 μm) radical capturing layer proved feasible by determining the appropriate slurry viscosity, spray head selection, and optimization of spraying conditions.


Author(s):  
Alexandre B. Andrade ◽  
Martha L. Mora Bejarano ◽  
Edgar F. Cunha ◽  
Eric Robalinho ◽  
Marcelo Linardi

A sieve printing technique has been developed for the preparation of gas diffusion electrodes for proton exchange membrane fuel cells (PEMFCs). The results of the preparation of membrane electrode assemblies (MEAs) are shown to be faster and highly reproducible by using the sieve printing and hot pressing method. These results were compared with those obtained by spray and hot pressing method. The experiments were carried out in a 25 cm2 single PEM fuel cell with platinum loadings of 0.4 mg Pt cm−2 and 0.6 mg Pt cm−2 on the anode and cathode, respectively. Scanning electron microscopy analysis was used to investigate the electrodes’ morphology. The performance of the MEAs was measured by polarization curves. It was observed that the sieve printing technique is highly reproducible and significantly more accurate and faster than the spray one. Sieve printing technique can be easily scaled up and is very adequate for high volume production with low-cost. Such features allow manufacturing large active areas for power stack fabrication. In addition, this deposition technique has produced MEAs with a 39.8% higher power density at 0.6 V when compared with the spray one.


2006 ◽  
Vol 161 (1) ◽  
pp. 275-281 ◽  
Author(s):  
Yi-Hao Pai ◽  
Jyh-Harng Ke ◽  
Hsin-Fu Huang ◽  
Chih-Ming Lee ◽  
Jyh-Myng Zen ◽  
...  

2021 ◽  
Vol 12 (1) ◽  
Author(s):  
Julius Knöppel ◽  
Maximilian Möckl ◽  
Daniel Escalera-López ◽  
Kevin Stojanovski ◽  
Markus Bierling ◽  
...  

AbstractRecent research indicates a severe discrepancy between oxygen evolution reaction catalysts dissolution in aqueous model systems and membrane electrode assemblies. This questions the relevance of the widespread aqueous testing for real world application. In this study, we aim to determine the processes responsible for the dissolution discrepancy. Experimental parameters known to diverge in both systems are individually tested for their influence on dissolution of an Ir-based catalyst. Ir dissolution is studied in an aqueous model system, a scanning flow cell coupled to an inductively coupled plasma mass spectrometer. Real dissolution rates of the Ir OER catalyst in membrane electrode assemblies are measured with a specifically developed, dedicated setup. Overestimated acidity in the anode catalyst layer and stabilization over time in real devices are proposed as main contributors to the dissolution discrepancy. The results shown here lead to clear guidelines for anode electrocatalyst testing parameters to resemble realistic electrolyzer operating conditions.


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