Hydrotreating of crude 2-ethylhexanol over Ni/Al2O3 catalysts: Surface Ni species-catalytic activity correlation

被引:81
作者
Yang, Renchun [1 ]
Li, Xiaogang [1 ]
Wu, Junsheng [1 ]
Zhang, Xin [1 ]
Zhang, Zhihua [1 ,2 ]
Cheng, Yufeng [3 ]
Guo, Jintao [2 ]
机构
[1] Univ Sci & Technol Beijing, Adv Mat & Technol Inst, Beijing 100083, Peoples R China
[2] PetroChina Daqing Res Ctr Chem Engn, Daqing 163714, Peoples R China
[3] Univ Calgary, Dept Mech & Mfg Engn, Calgary, AB T2N 1N4, Canada
关键词
Ni/gamma-Al2O3; Ni species; Reducibility; Hydrotreating; 2-Ethylhexanol; SUPPORTED NICKEL-CATALYSTS; SPHERICAL CATALYSTS; HYDROGEN-PRODUCTION; PHTHALIC-ANHYDRIDE; ALUMINA CATALYSTS; PARTIAL OXIDATION; PERFORMANCE; ETHANOL; OXIDE; NI/GAMMA-AL2O3;
D O I
10.1016/j.apcata.2009.08.021
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
A series of supported Ni/gamma-Al2O3 samples were prepared and then used to identify the surface Ni species. The samples were characterized by ICP-AES, XRD, TPR, and XPS. The results indicated that two types of Ni species occurred on the samples with Ni loading < 9.1 wt%, while four types of Ni species occurred on the samples with Ni loading > 9.1 wt%. The reduction temperatures around 350, 500-520, 620-650, and 750-800 degrees C corresponding to Ni species were related to amorphous NiO, crystal NiO, NiAl2O4, and NiAlxOy (x > 2), respectively. A correlation was made between the catalytic activities and the surface Ni species. For the catalysts that were difficult to reduce (Ni loading < 9.1 wt%), the activities were very poor at low reduction temperatures: for the easily reducible catalysts (Ni loading > 9.1 wt%), the activities were excellent in a wider reduction temperature range from 400 to 800 degrees C. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:105 / 112
页数:8
相关论文
共 43 条
[1]   Synthesis, characterization and performance evaluation of Ni/Al2O3 catalysts for reforming of crude ethanol for hydrogen production [J].
Akande , AJ ;
Idem, RO ;
Dalai, AK .
APPLIED CATALYSIS A-GENERAL, 2005, 287 (02) :159-175
[2]   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
[3]   Esterification of phthalic anhydride with 1-butanol and 2-ethylhexanol catalyzed by heteropolyacids [J].
Arabi, M ;
Amini, MM ;
Abedini, M ;
Nemati, A ;
Alizadeh, M .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2003, 200 (1-2) :105-110
[4]   Effects of small MoO3 additions on the properties of nickel catalysts for the steam reforming of hydrocarbons -: III.: Reduction of Ni-Mo/Al2O3 catalysts [J].
Borowiecki, T ;
Gac, W ;
Denis, A .
APPLIED CATALYSIS A-GENERAL, 2004, 270 (1-2) :27-36
[5]   Effect of thermal treatments on catalyst reducibility and activity in nickel supported on RHA-Al2O3 systems [J].
Chang, FW ;
Tsay, MT ;
Kuo, MS .
THERMOCHIMICA ACTA, 2002, 386 (02) :161-172
[6]   INTERACTION OF NICKEL IONS WITH A GAMMA-AL2O3 SUPPORT DURING DEPOSITION FROM AQUEOUS-SOLUTION [J].
DEBOKX, PK ;
WASSENBERG, WBA ;
GEUS, JW .
JOURNAL OF CATALYSIS, 1987, 104 (01) :86-98
[7]   Autothermal reforming of methane over Ni/γ-Al2O3 promoted with Pd The effect of the Pd source in activity, temperature profile of reactor and in ignition [J].
Dias, Joelmir A. C. ;
Assaf, Jose M. .
APPLIED CATALYSIS A-GENERAL, 2008, 334 (1-2) :243-250
[8]   SURFACE AREA AND PORE STRUCTURE OF NICKEL OXIDE [J].
FAHIM, RB ;
ABUSHADY, AI .
JOURNAL OF CATALYSIS, 1970, 17 (01) :10-&
[9]   Production of hydrogen by steam reforming of ethanol over Ni/Al2O3 spherical catalysts [J].
Fajardo, HV ;
Probst, LFD .
APPLIED CATALYSIS A-GENERAL, 2006, 306 :134-141
[10]  
FIEVET F, 1975, J CATAL, V39, P350