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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

邮发代号 80-969

2019 Impact Factor: 3.552

Frontiers of Chemical Science and Engineering  2014, Vol. 8 Issue (2): 161-170   https://doi.org/10.1007/s11705-014-1430-1
  本期目录
Hydrotreating of light gas oil using a NiMo catalyst supported on activated carbon produced from fluid petroleum coke
N. Rambabu1,Sandeep Badoga1,Kapil K. Soni1,A.K. Dalai1,*(),J. Adjaye2
1. Catalysis and Chemical Reaction Engineering Laboratories, Department of Chemical and Biological Engineering, University of Saskatchewan, Saskatoon, SK, S7N 5A9, Canada
2. Syncrude Edmonton Research Centre, Edmonton, AB, T6N 1H4, Canada
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Abstract

Nitric acid functionalized steam activated carbon (NAFSAC) was prepared from waste fluid petroleum coke (FPC) and used as a support material for the synthesis of a NiMo catalyst (2.5 wt-% Ni and 13 wt-% Mo). The catalyst was then used for the hydrotreatment of light gas oil. The support and catalysts were characterized by Brunauer-Emmett-Teller (BET) gas adsorption method, X-ray diffraction, H2-temperature programmed reduction, NH3-temperature programmed desorption, CO-chemisorption, mass spetrography, scanning electron microscopy (SEM), Boehm titration, and Fourier transform infrared spectroscopy (FTIR). The SEM results showed that the carbon material retained a needle like structure after functionalization with HNO3. The Boehm titration, FTIR, and BET results confirmed that the HNO3 functionalized material had moderate acidity, surface functional groups, and mesoporosity respectively. The produced NAFSAC had an inert nature, exhibited the sink effect and few metal support interactions, and contained functional groups. All of which make it a suitable support material for the preparation of a NiMo hydrotreating catalyst. Hydrotreating activity studies of the NiMo/NAFSAC catalyst were carried out under industrial operating conditions in a laboratory trickle bed reactor using coker light gas oil as the feedstock. A parallel study was performed on the hydrotreating activity of NiMo/γ-Al2O3 as a reference catalyst. The hydrodesulfurization and hydrodenitrogenation activities of the NiMo/NAFSAC catalyst were 62% and 30%, respectively.

Key wordsactivated carbon    fluid petroleum coke    NiMo catalyst    hydrotreating    light gas oil
收稿日期: 2013-12-30      出版日期: 2014-05-22
Corresponding Author(s): A.K. Dalai   
 引用本文:   
. [J]. Frontiers of Chemical Science and Engineering, 2014, 8(2): 161-170.
N. Rambabu,Sandeep Badoga,Kapil K. Soni,A.K. Dalai,J. Adjaye. Hydrotreating of light gas oil using a NiMo catalyst supported on activated carbon produced from fluid petroleum coke. Front. Chem. Sci. Eng., 2014, 8(2): 161-170.
 链接本文:  
https://academic.hep.com.cn/fcse/CN/10.1007/s11705-014-1430-1
https://academic.hep.com.cn/fcse/CN/Y2014/V8/I2/161
SampleBET surface area /m2·g–1Total pore volume /cm3·g–1Average pore diameter /Å
RFC11.7--
SAC482.00.23137.1
NAFSAC280.00.29741.0
NiMo/NAFSAC900.339.0
Tab.1  
Fig.1  
SampleAcidic functional groups concentration /mmol·g–1
RFC1.625
SAC0.752
NAFSAC2.410
Tab.2  
Fig.2  
Fig.3  
Fig.4  
CatalystMetal Dispersion /%Metallic surface area /m2/g, of sampleMetallic surface area /m2/g, of metalCrystallite size /nmCO adsorbed /μmol/g
NiMo/NAFSAC4.43.421.62878
NiMo/γ-Al2O39.57.8357.913182
Tab.3  
Fig.5  
Fig.6  
CharacteristicCoker light gas oil
Nitrogen /ppm2439
Sulfur /ppm23420
Density /g·mL–10.95
Boiling point distribution
IBP /°C169
FBP /°C548
Boiling range /°C
IBP–2506
250-30022
300-35031
350-40023
401-4509
450-5006
500–FBP3
Tab.4  
Fig.7  
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