Deactivation mechanism and regeneration study of Zn/HZSM-5 catalyst in ethylene transformation

被引:22
作者
Bonnin, Aurelien [1 ]
Pouilloux, Yannick [1 ]
Coupard, Vincent [2 ]
Uzio, Denis [2 ]
Pinard, Ludovic [1 ]
机构
[1] CNRS, Inst Chim Milieux & Mat Poitiers IC2MP, UMR 7285, 4 Rue Michel Brunet,Batiment B27,TSA 51106, F-86073 Poitiers 9, France
[2] IFP Energies Nouvelles, Etab Lyon, Rond Point Echangeur Solaize BP 3, F-69360 Solaize, France
关键词
Zn/H-ZSM-5; Ethylene; Deactivation; Coke; Lewis and Bronsted acid sites;
D O I
10.1016/j.apcata.2020.117976
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
The purpose of this study is to identify the deactivation mechanism(s) that occurs during the aromatization of dilute ethylene at 500 degrees C on Zn/H-MFI catalyst. More than 15 catalysts, with a Zn/H+ molar ratio ranging from 0 (H-ZSM5) to 1.8 (Zn/H-ZSM5), were prepared by wet impregnation. Deactivation does not result from Zn sublimation, but from coking. The deactivation function and coke deposition can be modelled by simple exponential laws. Moreover, the balance between Lewis (Zn) and Bronsted (H+) acid sites is a good descriptor for predicting the catalyst stability. The coke poisoning has a similar impact on the diminution of micropore volume as well as on the reduction of the number of Lewis and Bronsted acid sites. The best suited descriptor for describing deactivation is the reduction of the micropore volume.
引用
收藏
页数:13
相关论文
共 38 条
[1]   INFLUENCES OF COPPER ON PHYSICOCHEMICAL AND CATALYTIC PROPERTIES OF ZSM-5 ZEOLITES IN THE REACTION OF ETHENE AROMATIZATION [J].
ARISHTIROVA, K ;
DIMITROV, C ;
DYREK, K ;
HALLMEIER, KH ;
POPOVA, Z ;
WITKOWSKI, S .
APPLIED CATALYSIS A-GENERAL, 1992, 81 (01) :15-26
[2]  
Asaftei IV, 2015, REV CHIM-BUCHAREST, V66, P963
[3]   Mechanism and Kinetic of Coke Oxidation by Nonthermal Plasma in Fixed-Bed Dielectric Barrier Reactor [J].
Astafan, A. ;
Batiot-Dupeyrat, C. ;
Pinard, L. .
JOURNAL OF PHYSICAL CHEMISTRY C, 2019, 123 (14) :9168-9175
[4]   Particular properties of the coke formed on nano-sponge *BEA zeolite during ethanol-to-hydrocarbons transformation [J].
Astafan, A. ;
Benghalem, M. A. ;
Pouilloux, Y. ;
Patarin, J. ;
Bats, N. ;
Bouchy, C. ;
Daou, T. J. ;
Pinard, L. .
JOURNAL OF CATALYSIS, 2016, 336 :1-10
[5]   Mechanisms of catalyst deactivation [J].
Bartholomew, CH .
APPLIED CATALYSIS A-GENERAL, 2001, 212 (1-2) :17-60
[6]   Determination of the Exact Microporous Volume and BET Surface Area in Hierarchical ZSM-5 [J].
Batonneau-Gener, Isabelle ;
Sachse, Alexander .
JOURNAL OF PHYSICAL CHEMISTRY C, 2019, 123 (07) :4235-4242
[7]   A fundamental kinetic model for the catalytic cracking of alkanes on a USY zeolite in the presence of coke formation [J].
Beirnaert, HC ;
Alleman, JR ;
Marin, GB .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2001, 40 (05) :1337-1347
[8]   Structure and density of active Zn species in Zn/H-ZSM5 propane aromatization catalysts [J].
Biscardi, JA ;
Meitzner, GD ;
Iglesia, E .
JOURNAL OF CATALYSIS, 1998, 179 (01) :192-202
[9]   Influence of coke on the acid properties of a USHY zeolite [J].
Cerqueira, HS ;
Ayrault, P ;
Datka, J ;
Guisnet, M .
MICROPOROUS AND MESOPOROUS MATERIALS, 2000, 38 (2-3) :197-205
[10]   Mechanisms of coke growth on mordenite zeolite [J].
Chaouati, N. ;
Soualah, A. ;
Chater, M. ;
Tarighi, M. ;
Pinard, L. .
JOURNAL OF CATALYSIS, 2016, 344 :354-364