Effect of the preparation method on particle size and reaction selectivity on naphthalene hydrogenation over Ni/H-MOR catalysts

被引:19
作者
Cuevas-Garcia, R. [1 ]
Tellez-Romero, J. G. [1 ]
Ramirez, J. [1 ]
Sarabia-Banuelos, P. [1 ]
Puente-Lee, I. [3 ]
Salcedo-Luna, C. [3 ]
Hernandez-Gonzalez, S. [2 ]
Nolasco-Arizmendi, V. A. [2 ]
机构
[1] Univ Nacl Autonoma Mexico, Fac Quim, Dept Ingn Quim, UNICAT, Ciudad Univ, Mexico City 04510, DF, Mexico
[2] Univ Tecnol Tula Tepeji, Ave Univ Tecnol 1000, Tula De Allende 42830, Hidalgo, Mexico
[3] Univ Nacl Autonoma Mexico, Fac Quim, USAII, Ciudad Univ, Mexico City 04510, DF, Mexico
基金
芬兰科学院;
关键词
Ni/H-MOR catalyst; Naphthalene hydrogenation; Catalyst deactivation;
D O I
10.1016/j.cattod.2019.08.044
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Three Ni catalyst supported on mordenite zeolite with the same content of nickel, similar to 2 wt.%, were prepared by incipient wetness impregnation (IWI), ionic exchange (IE), and deposition-precipitation (DP) methods. The catalysts were characterized by, X-ray diffraction (XRD), textural properties, temperature-programmed reduction (TPR), transmission electron microscopy (TEM) and scanning electron microscopy / energy-dispersive spectroscopy (SEM/EDS). For all the catalysts conversion and selectivity were studied in naphthalene hydrogenation without or with thiophene in the feedstock. Despite the low nickel content, the three preparations showed a high initial total naphthalene conversion up to 94%. The Ni-IWI catalyst exhibited high selectivity to tetralin and deactivated very fast. Ni-IE catalyst had good activity; however, it shows deactivation and the main products are related to acid reactions. The Ni-DP shows high hydrogenation activity and was the most active catalyst, it generated decalins, especially cis-decalin and at a long reaction time on stream, the catalyst remains active. TEM and TPR results suggest that this behavior is related to the crystal sizes which in turn is conected with the preparation method. In presence of thiophene, all the catalysts deactivate; but the Ni-DP deactivation was slower.
引用
收藏
页码:63 / 71
页数:9
相关论文
共 45 条
[1]   Hydrogenation of naphthalene on NiMo- Ni- and Ru/Al2O3 catalysts:: Langmuir-Hinshelwood kinetic modelling [J].
Alves Monteiro-Gezork, Ana Cristina ;
Natividad, Reyna ;
Winterbottom, John Mike .
CATALYSIS TODAY, 2008, 130 (2-4) :471-485
[2]  
[Anonymous], 2007, ATLAS ZEOLITE STRUCT
[3]   Science and technology of novel processes for deep desulfurization of oil refinery streams: A review [J].
Babich, IV ;
Moulijn, JA .
FUEL, 2003, 82 (06) :607-631
[4]  
Bartholomew C.H., 2019, STUD SURF SCI CAT, V34, P81
[5]  
Bartholomew C.H., 2019, J ADV CATAL, V31, P135
[6]   Mechanisms of catalyst deactivation [J].
Bartholomew, CH .
APPLIED CATALYSIS A-GENERAL, 2001, 212 (1-2) :17-60
[7]   Aromatics reduction of pyrolysis gasoline (PyGas) over HY-supported transition metal catalysts [J].
Castano, P. ;
Pawelec, B. ;
Fierro, J. L. G. ;
Arandes, J. M. ;
Bilbao, J. .
APPLIED CATALYSIS A-GENERAL, 2006, 315 :101-113
[8]   Aromatic saturation of distillates: An overview [J].
Cooper, BH ;
Donnis, BBL .
APPLIED CATALYSIS A-GENERAL, 1996, 137 (02) :203-223
[9]   Bioethanol steam reforming on Ni-based modified mordenite. Effect of mesoporosity, acid sites and alkaline metals [J].
Da Costa-Serra, J. F. ;
Navarro, M. T. ;
Rey, F. ;
Chica, A. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2012, 37 (08) :7101-7108
[10]   Comparative study of the hydrogenation of tetralin on supported NiPt, and Pd catalysts [J].
Dokjampa, Siraprapha ;
Rirksomboon, Thirasak ;
Osuwan, Somchai ;
Jongpatiwut, Siriporn ;
Resasco, Daniel E. .
CATALYSIS TODAY, 2007, 123 (1-4) :218-223