Activity and degradation of Pt/Al2O3 catalyst assessment in hydrogen release from perhydro-dibenzyltoluene

被引:0
|
作者
Tardio, Carlos [1 ]
Rodriguez, Jesus [1 ]
Montes, Cristina [1 ]
Buchaca, Marc Martinez de Sarasa [2 ]
Lopez-Montenegro, Sheila [3 ]
Esteban, Cristina [3 ]
Gomez, Felix [3 ]
Campana, Roberto [1 ]
机构
[1] Ctr Nacl Hidrogeno, Prolongac Fernando Santo S-N, Ciudad Real 13500, Spain
[2] Univ Castilla La Mancha, Fac Ciencias & Tecnol Quim, Dept Ingn Quim Organ & Bioquim, Ctr Innovac Quim Avanzada ORFEO CINQA, Ciudad Real 13071, Spain
[3] Exolum Solut, Titan 13, Madrid 28045, Spain
关键词
LOHC; Hydrogen storage; Perhydro-dibenzyltoluene; Pt/Al2O3; catalyst; Dehydrogenation; Catalytic stress; CARRIER SYSTEMS; DEHYDROGENATION; STORAGE; LOHC; SIZE; COMBUSTION; STABILITY; AMMONIA; DECALIN; MODEL;
D O I
10.1016/j.ijhydene.2024.09.072
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
Liquid organic hydrogen carrier (LOHC) is a hydrogen storage and release technology of growing interest due to its excellent properties. Dibenzyltoluene is one of the best performing organic liquids for this purpose. In this work, we investigate the dehydrogenation reaction of perhydro-dibenzyltoluene (18H-DBT) in a batch reactor using Pt/Al2O3 catalysts. The best catalytic results were obtained at 290 degrees C with the catalyst featuring lower Pt loading and higher dispersion, achieving a degree of dehydrogenation (DoD) of 88%. After 45 h of catalytic operation, the degree of dehydrogenation dropped by about 35%. The generation of by-products and physical changes in the Pt sites could be potential causes of the observed catalytic degradation. A cleaning treatment was carried out to restore the initial DoD, but only the productivity was improved, leading to a reduction in reaction times.
引用
收藏
页码:1453 / 1460
页数:8
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