Enhancing the power density of hydrogen release from LOHC systems by high Pt loadings on hierarchical alumina support structures

被引:1
作者
Auer, Franziska [1 ]
Solymosi, Thomas [1 ]
Erhardt, Chris [1 ,2 ]
Collados, Carlos Cuadrado [3 ]
Thommes, Matthias [3 ]
Wasserscheid, Peter [1 ,2 ,4 ]
机构
[1] Helmholtz Inst Erlangen Nurnberg Energy Technol IE, Erlangen, Germany
[2] Friedrich Alexander Univ Erlangen Nurnberg FAU, Lehrstuhl Chem Reaktionstechn, Erlangen, Germany
[3] Friedrich Alexander Univ Erlangen Nurnberg FAU, Lehrstuhl Therm Verfahrenstechn, Erlangen, Germany
[4] Forschungszentrum Julich GmbH, Inst Sustainable Hydrogen Econ INW, Julich, Germany
关键词
LOHC; Dehydrogenation; Space-time-yield; Power-density; Reactor; Catalyst; CARRIER SYSTEMS; STORAGE; TRANSPORT; EFFICIENT;
D O I
10.1016/j.ijhydene.2024.12.155
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
In this contribution, a step change in the power density of hydrogen release from LOHC systems is presented. This could be achieved by the use of hierarchical alumina supports in combination with high Pt loadings. Here, a demonstration was carried out for the catalytic dehydrogenation of perhydro dibenzyltoluene (H18-DBT). In the course of our study, different alumina support materials were characterized and loaded with 0.3, 0.6, 0.9 and 1.2 wt%Pt, respectively. It was found that a specific bimodal pore structure with a large pore volume in both, the mesoporous range between 10 and 25 nm and the macroporous range between 500 and 1000 nm, enabled high Pt-based productivities even at Pt loadings, four times higher than that of the current technical standard. This gives access to a substantially improved volumetric power density of the respective catalyst. In batch dehydrogenation experiments with a 1.5 mm pellet and a Pt loading of 0.9 wt%Pt, a doubling of volumetric power density could be achieved compared to the technical 0.3 wt%Ptstandard material (Clariant, Elemax D102). Our analytical work elucidated that this highly relevant increase can be related to a faster mass transfer resulting from the special pore structure of the catalyst support and to a better Pt distribution on the support resulting in a thinner egg-shell layer. Using the optimized catalyst materials in continuous fixed-bed dehydrogenation experiments higher gas hold-up in the reactor and dewetting of the catalyst surface become additional aspects that influence the overall observed catalyst performance.
引用
收藏
页码:1282 / 1290
页数:9
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