Applied Catalysis B: Environmental 107 (2011) 59–67
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Applied Catalysis B: Environmental
jo ur n al homepage: www.elsevier.com/locate/apcatb
Effect of glycol on the formation of active species and sulfidation mechanism of
CoMoP/Al
2
O
3
hydrotreating catalysts
Thanh Son Nguyen
a
, Stéphane Loridant
a
, Lorentz Chantal
a
, Thierry Cholley
b
, Christophe Geantet
a,∗
a
Institut de Recherches sur la Catalyse et l’Environnement de Lyon (IRCELyon), UMR5256 CNRS – Université Lyon I, 2 avenue Albert Einstein, 69626 Villeurbanne cedex, France
b
Division Assistance Technique – Direction Technique – Total, BP 98-76700 Harfleur, France
a r t i c l e i n f o
Article history:
Received 20 April 2011
Received in revised form 17 June 2011
Accepted 24 June 2011
Available online 30 June 2011
Keywords:
Hydrotreating catalyst
Sulphidation
Additive
TEG
Raman spectroscopy
QEXAFS
27Al NMR
a b s t r a c t
The present work is focused on the role of an organic promoter (triethyleneglycol – TEG) on the activity of
hydrotreating catalysts. By impregnating such compound on oxidic industrial catalyst, an enhancement of
the catalytic activity in the HDS conversion of 4,6-DMDBT as well as SRGO HDS was obtained. Using several
physico-chemical techniques and in situ characterization (Raman, XAS), it was found that TEG affected
the coordination of Co and Mo in the oxidic species. During the activation procedure, the presence of TEG
slows down the sulfidation and allows the genesis of more active “CoMoS” species.
© 2011 Elsevier B.V. All rights reserved.
1. Introduction
In recent years, as legislation concerning the emission of sulfur-
containing pollutants is becoming stricter, the HDS process has to
be improved. One way to achieve this goal is to increase the activ-
ity of CoMo and NiMo hydrodesulfurization (HDS) catalysts with
new preparation routes or by adding doping agents. Several patents
claimed the unusual effect of organic additives on the activity of
hydrotreating catalysts [1–3]. Some of the organic compounds are
almost infinitely water soluble and can be added during the incip-
ient wetness impregnation of the active metals [2] or impregnated
directly on the oxidic form of the catalyst in a second step [3]. In
these patents, the organic additive is still present on the surface
of the catalyst when the sulfidation starts. Despite the important
number of industrial patents deposed in the last decade concerning
the use of glycol-type additives in HDS catalysts, these additives are
still a subject of current interest in the researches academic since no
general agreement exists about the origin of the beneficial influence
of these non chelating additives [4].
According to Nicosia and Prins [5,6], the catalyst impregnated
with solution containing TEG showed a higher catalytic activity
than the catalyst prepared without TEG. Raman and EXAFS spec-
∗
Corresponding author.
E-mail address: Christophe.Geantet@ircelyon.univ-lyon1.fr (C. Geantet).
troscopy demonstrated that the impregnation solution containing
the metal salts and phosphoric acid contained HP
2
Mo
5
O
23
5-
diphosphopentamolybdate and that this anion was not affected
by the presence of TEG.
31
P NMR measurements of the impregna-
tion solution showed a paramagnetic effect of cobalt, which proved
that cobalt is complexed by the diphosphopentamolybdate, both
in the presence and absence of TEG. Concerning the Mo species, by
mean of UV–Vis and Mo X-ray absorption, they suggested the exis-
tence of tetrahedral and octahedral coordination for molybdenum
in presence of glycol.
In the more recent study, Costa et al. [7] proposed the formation
of PCoMo
11
O
40
7-
species after additive impregnation in the case of
CoMoP dried catalysts (P/Mo molar ratio ≥ 0.4) by mean of Raman
spectroscopy characterization.
Regarding the role of glycol-type additives on the sulfida-
tion step, the academic literature showed controversial results.
Nicosia and Prins [5,6] studied catalysts prepared from MoO
3
,
H
3
PO
4
and CoCO
3
as reported in the literature [2]. EXAFS
experiments showed that in presence of glycols, the sulfidation
mechanism is modified and a faster sulfidation is observed. On
the other hand, Mazoyer-Galliou et al. [8] have investigated the
sulfidation of industrial calcined CoMo and CoMoP catalysts post-
impregnated with diethyleneglycol monobutyl ether (DEGbe).
They have shown, by elemental analysis on CoMo and DEGbe-
impregnated CoMo/alumina catalysts, that the global sulfidation is
delayed at temperature inferior to 473 K. In the same study, EXAFS
0926-3373/$ – see front matter © 2011 Elsevier B.V. All rights reserved.
doi:10.1016/j.apcatb.2011.06.037