Effect of fluorine addition on the formation of active species and hydrotreating activity of NiWS/Al2O3 catalysts
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Song, CJ
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Seoul Natl Univ, Sch Chem Engn, Inst Chem Proc, Kwanak Ku, Seoul 151744, South KoreaSeoul Natl Univ, Sch Chem Engn, Inst Chem Proc, Kwanak Ku, Seoul 151744, South Korea
Song, CJ
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Kwak, C
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Seoul Natl Univ, Sch Chem Engn, Inst Chem Proc, Kwanak Ku, Seoul 151744, South KoreaSeoul Natl Univ, Sch Chem Engn, Inst Chem Proc, Kwanak Ku, Seoul 151744, South Korea
Kwak, C
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Moon, SH
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Seoul Natl Univ, Sch Chem Engn, Inst Chem Proc, Kwanak Ku, Seoul 151744, South KoreaSeoul Natl Univ, Sch Chem Engn, Inst Chem Proc, Kwanak Ku, Seoul 151744, South Korea
Moon, SH
[1
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[1] Seoul Natl Univ, Sch Chem Engn, Inst Chem Proc, Kwanak Ku, Seoul 151744, South Korea
Fluorine-added Ni/Al2O3, W/Al2O3 and NiW/Al2O3 catalysts were prepared and their surface properties investigated using temperature-programmed reduction, diffuse reflectance spectroscopy and temperature-programmed sulfidation. The hydrodesulfurization (HDS) of thiophene was used as a model reaction to examine the activity of fluorinated NiW/Al2O3. Fluorination led to an increase in the formation of polymeric tungstates in W/Al2O3 and the surface nickel spinel species in the case of Ni/Al2O3. Fluorination promoted the sulfidation of the NiW/Al2O3 catalyst and the interaction of nickel with tungsten to produce the Ni-W-O species, a precursor of active catalytic sites. The activity of NiW/Al2O3 was increased by fluorination up to a fluorine content of 4 wt.%, and then decreased at higher fluorine contents. Two opposite effects of fluorination determine the characteristic changes in the activity of NiW/Al2O3: the enhanced sulfidation of the catalyst and incorporation of nickel with tungsten, both of which promote the activity, and a decrease in the dispersion of active species, which lowers the activity. The activity results obtained in this study are different from those reported previously [Appl. Catal. A 144 (1996) 343], suggesting that the extent of catalyst modification by fluorination is strongly dependent on the conditions of catalyst preparation. (C) 2002 Elsevier Science B.V. All rights reserved.
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Samara State Tech Univ, 244 Molodogvardiyskaya St, Samara 443100, Russia
All Russia Res Inst Oil Refining JSC VNII NP JSC, Aviamotornaya St 6, Moscow 111116, RussiaSamara State Tech Univ, 244 Molodogvardiyskaya St, Samara 443100, Russia
Minaev, Pavel
Nikulshina, Maria
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Samara State Tech Univ, 244 Molodogvardiyskaya St, Samara 443100, RussiaSamara State Tech Univ, 244 Molodogvardiyskaya St, Samara 443100, Russia
Nikulshina, Maria
Mozhaev, Alexander
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Samara State Tech Univ, 244 Molodogvardiyskaya St, Samara 443100, RussiaSamara State Tech Univ, 244 Molodogvardiyskaya St, Samara 443100, Russia
Mozhaev, Alexander
Maslakov, Konstantin
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Lomonosov Moscow State Univ, Fac Chem, GSP-1,Leninskie Gory 1-1, Moscow 119991, RussiaSamara State Tech Univ, 244 Molodogvardiyskaya St, Samara 443100, Russia
Maslakov, Konstantin
Boldushevskii, Roman
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Lomonosov Moscow State Univ, Fac Chem, GSP-1,Leninskie Gory 1-1, Moscow 119991, RussiaSamara State Tech Univ, 244 Molodogvardiyskaya St, Samara 443100, Russia
Boldushevskii, Roman
Nikulshin, Pavel
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Samara State Tech Univ, 244 Molodogvardiyskaya St, Samara 443100, Russia
All Russia Res Inst Oil Refining JSC VNII NP JSC, Aviamotornaya St 6, Moscow 111116, RussiaSamara State Tech Univ, 244 Molodogvardiyskaya St, Samara 443100, Russia