Experimental study of the oxidative steam reforming of fuel grade bioethanol over Pt-Ni metallic foam structured catalysts

被引:6
|
作者
Ruocco, Concetta [1 ]
Coppola, Antonio [1 ]
Picciotti, Gianmario [2 ]
Palma, Vincenzo [1 ]
机构
[1] Univ Salerno, Dept Ind Engn, Via Giovanni Paolo II 132, I-83040 Fisciano, SA, Italy
[2] Eldor Corp SpA, Via Don Paolo Berra 18, I-22030 Orsenigo, CO, Italy
关键词
Platinum; Ceria; Fuel grade ethanol; Coke; Foam; CRUDE BIO-ETHANOL; HYDROGEN-PRODUCTION; NI/AL2O3; CATALYSTS; METHANE; INTENSIFICATION; FERMENTATION; TEMPERATURE; NI/SIO2; SURFACE; NICKEL;
D O I
10.1016/j.ijhydene.2022.05.276
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 work, Pt-Ni/CeO2 catalysts have been used for the oxidative steam reforming of fuel grade bioethanol. To transfer the above formulation on structured carriers, due to the requirement of a washcoat (wc) deposition, it was mandatory to carry out a preliminary study on the catalysts in the form of powder. An initial experimental campaign was per-formed to optimise the ceria loading (between 25 and 45 wt%) as well as the Pt content (between 2 and 5 wt%): stability tests were carried out for 24 h at 500 degrees C, WHSV = 12.3 h-1, H2O/C2H5OH ratio of 4, O2/C2H5OH of 0.5. The highest activity, selectivity and durability was recorded over the 3Pt-10Ni/35CeO2/wc, which assured an ethanol conversion of almost 98% at the end of the test with a corresponding H2 yield of 50%. This interesting formu-lation was transferred on a Ni-Fe substrate, made of an open cell foam, which was tested under the same operative conditions described above: the structured catalyst, due to the very good heat management within the catalytic bed and the improved mass transport, displayed a more stable behaviour compared to the corresponding powder, even in the presence of the typical bioethanol impurities; moreover, the formation of unwanted by-products was negligible throughout the whole investigated interval. (c) 2022 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:11943 / 11955
页数:13
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