2015
DOI: 10.1016/j.cattod.2014.06.029
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Catalyst development for the dehydrogenation of MCH in a microstructured membrane reactor—For heat storage by a Liquid Organic Reaction Cycle

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Cited by 28 publications
(14 citation statements)
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“…Very early on, modifiers were added to avoid secondary reactions of cracking and isomerization leading to the formation of coke [10]. It has also been established that the presence of hydrogen in the gas phase prevents the deactivation of Pd nanoparticles by suppressing coke formation, in contrast to what has been observed in the absence of hydrogen [52][53][54]. In a study of toluene hydrogenation on Pt/Al 2 O 3 , Taimoor and Pitault [55] observed a slow and reversible deactivation even in the presence of hydrogen and demonstrated that this was due to a strong adsorption of toluene on alumina.…”
Section: Catalystsmentioning
confidence: 99%
“…Very early on, modifiers were added to avoid secondary reactions of cracking and isomerization leading to the formation of coke [10]. It has also been established that the presence of hydrogen in the gas phase prevents the deactivation of Pd nanoparticles by suppressing coke formation, in contrast to what has been observed in the absence of hydrogen [52][53][54]. In a study of toluene hydrogenation on Pt/Al 2 O 3 , Taimoor and Pitault [55] observed a slow and reversible deactivation even in the presence of hydrogen and demonstrated that this was due to a strong adsorption of toluene on alumina.…”
Section: Catalystsmentioning
confidence: 99%
“…In addition to the aforementioned CMR types, researchers also explored alternative modules and operating conditions. Kreuder et al [98] prepared various catalysts with Pt and Pt-Sn as the active material and Al 2 O 3 prepared by different ways and also CeO 2 -ZrO 2 as the support materials, with catalysts coated on the wall of thin foils inside a microstructured reactor, and compared their performances. They found that 1 wt% Pt/Al 2 O 3 showed the best performance but reported fast deactivation of catalysts by carbon formation on the catalyst surface at normal pressure (~1 bar).…”
Section: Catalytic Membrane Reactormentioning
confidence: 99%
“…Pd-based membrane reactors have already been developed for the dehydrogenation of LOHC methylcyclohexane, and the steam reforming of methane, where promising results could be achieved [3,8,9,72,73,74,75]. For adaptation to the multiphase system 18H-DBT/0H-DBT/H 2 , a multi-stage reactor concept with intermediate separation of hydrogen was developed.…”
Section: Process Intensification In Lohc Dehydrogenation Using Pd-mentioning
confidence: 99%