Hydrogen and fuel cell catalyst maker Pajarito Powder receives Series-B investment from Hyundai Motor

2021 ◽  
Vol 2021 (10) ◽  
pp. 6
Keyword(s):  
2020 ◽  
Vol 12 (15) ◽  
pp. 17602-17610 ◽  
Author(s):  
Ivan Khalakhan ◽  
Marco Bogar ◽  
Mykhailo Vorokhta ◽  
Peter Kúš ◽  
Yurii Yakovlev ◽  
...  

2017 ◽  
Vol 23 (S1) ◽  
pp. 2090-2091
Author(s):  
Brian T. Sneed ◽  
David A. Cullen ◽  
Kimberly S. Reeves ◽  
Karren L. More

2021 ◽  
Author(s):  
Johanna Schröder ◽  
Rebecca K. Pittkowski ◽  
Isaac Martens ◽  
Raphaël Chattot ◽  
Jakub Drnec ◽  
...  

The combination of operando small- and wide-angle X-ray scattering (SAXS, WAXS) is here presented to provide insights into the changes in mean particle sizes and phase fractions in fuel cell catalyst layers during accelerated stress tests (ASTs). As fuel cell catalyst, a bimodal Pt/C catalyst was chosen that consists of two distinguishable particle size populations. The presence of the two different sizes should favor and uncover electrochemical Ostwald ripening as degradation mechanism, i.e., the growth of larger particles in the Pt/C catalyst at the expense of the smaller particles via the formation of ionic metal species. However, instead of electrochemical Ostwald ripening, the results point toward classical Ostwald ripening via the local diffusion of metal atoms on the support. Furthermore, the grazing incidence mode provides insights into the catalyst layer depth-dependent degradation. While the larger particles show the same particle size changes close to the electrolyte-catalyst interface and within the catalyst layer, the smaller Pt nanoparticles exhibit a slightly decreased size at the electrolyte-catalyst interface. During the AST, both size populations increase in size, independent of the depth. Their phase fraction, i.e., the ratio of smaller to larger size population, however, exhibits a depth-dependent behavior. While at the electrolyte-catalyst interface the phase fraction of the smaller size population decreases, it increases in the inner catalyst layer. The results of a depth-dependent degradation suggest that employing a depth-dependent catalyst design can be used for future improvement of catalyst stability.


2018 ◽  
Vol 165 (11) ◽  
pp. F1012-F1018 ◽  
Author(s):  
Scott A. Mauger ◽  
K. C. Neyerlin ◽  
Ami C. Yang-Neyerlin ◽  
Karren L. More ◽  
Michael Ulsh

2012 ◽  
Vol 124 (28) ◽  
pp. 7104-7107 ◽  
Author(s):  
Patraporn Luksirikul ◽  
Karaked Tedsree ◽  
Mark G. Moloney ◽  
Malcolm L. H. Green ◽  
Shik Chi Edman Tsang

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