2015
DOI: 10.1016/j.ijhydene.2014.11.151
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Structured nanocomposite catalysts of biofuels transformation into syngas and hydrogen: Design and performance

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Cited by 27 publications
(19 citation statements)
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References 26 publications
(45 reference statements)
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“…There are several approaches to the preparation of catalysts with a high specific surface area based on the oxides of a perovskite structure. One of the possible ways is to fix the active component on the surface of an inert oxide or to introduce it into ceramic/cermet foamy supports [7]. Another method to obtain the sample of a high specific surface area is template synthesis, which includes the use of a high surface area template at the precursor compound formation stage [8].…”
Section: Introductionmentioning
confidence: 99%
“…There are several approaches to the preparation of catalysts with a high specific surface area based on the oxides of a perovskite structure. One of the possible ways is to fix the active component on the surface of an inert oxide or to introduce it into ceramic/cermet foamy supports [7]. Another method to obtain the sample of a high specific surface area is template synthesis, which includes the use of a high surface area template at the precursor compound formation stage [8].…”
Section: Introductionmentioning
confidence: 99%
“…Liu and Lin [19,20] studied glycerol ATR on coated forms of LaMnO 3 and LaNiO 3 perovskites in monolith reactors and found that the latter favored H 2 production, which was possible on LaMnO 3 by Pt promotion to give ∼60% and ∼40% selectivity towards H 2 and CO, respectively. Use of structured reactors for glycerol ATR was also studied by Sadykov et al [21,22]. The authors tested Ni-Ru catalyst integrated to a metallic substrate with high thermal conductivity, and observed near equilibrium syngas yields with no transport resistances.…”
Section: Introductionmentioning
confidence: 99%
“…The authors tested Ni-Ru catalyst integrated to a metallic substrate with high thermal conductivity, and observed near equilibrium syngas yields with no transport resistances. They also emphasized the importance of optimizing the amount of O 2 in the feed for improving catalyst stability via reduced coking [22]. Oxidative conversion of glycerol in the absence and presence of inlet H 2 O vapor was studied at 900-1200°C and C/O = 0.8-1.6 in a different catalyst geometry dictated by α-Al 2 O 3 foam on which Rh-Ce/γ-Al 2 O 3 was washcoated [23].…”
Section: Introductionmentioning
confidence: 99%
“…Другим перспективным применением ВПЯМ системы Fe-Cr-Al являются структурированные носители катализаторов для превращения природного газа и биотоплива в сингаз и водород [4] и глубокого окисления метана [5,6]. Рабочие температуры ВПЯМ-хромаль при этом лежат в среднем интервале температур (600…800 °C), где они могут конкурировать с материалами аналогичной структуры на основе керамик [7].…”
Section: Introductionunclassified