Guaiacol derivatives and inhibiting species adsorption over MoS2 and CoMoS catalysts under HDO conditions: A DFT study

Abstract We have investigated using DFT calculations the η1 adsorption of guaiacol, phenol, anisole and phenol over CoMoS and MoS2 phases under HDO conditions. This adsorption mode should lead to a direct deoxygenation (DDO) reaction, which is low hydrogen-consuming. The most stable mode is an adsorption through the OH group of the molecule. The calculation of adsorption Gibbs free energies of inhibiting compounds (H2O, H2S, and CO) which can be present under reaction conditions shows that these molecules adsorb more strongly than oxygenated compounds, which suggests that CO will be a major inhibitor of the HDO process of real feeds.

[1]  G. Kresse,et al.  Ab initio molecular dynamics for liquid metals. , 1993 .

[2]  Christophe Geantet,et al.  Co-processing of pyrolisis bio oils and gas oil for new generation of bio-fuels: Hydrodeoxygenation of guaïacol and SRGO mixed feed , 2009 .

[3]  C. Geantet,et al.  Impact of Oxygenated Compounds from Lignocellulosic Biomass Pyrolysis Oils on Gas Oil Hydrotreatment , 2009 .

[4]  A. Krause,et al.  Hydrodeoxygenation of methyl esters on sulphided NiMo/γ-Al2O3 and CoMo/γ-Al2O3 catalysts , 2005 .

[5]  Y. Romero,et al.  Hydrodeoxygenation of 2-ethylphenol as a model compound of bio-crude over sulfided Mo-based catalysts: Promoting effect and reaction mechanism , 2010 .

[6]  J. Adjaye,et al.  On the incorporation of nickel and cobalt into MoS2-edge structures , 2004 .

[7]  A. Krause,et al.  Effect of H2S on the stability of CoMo/Al2O3 catalysts during hydrodeoxygenation , 2000 .

[8]  P. Raybaud,et al.  Promoter Sensitive Shapes of Co(Ni)MoS Nanocatalysts in Sulfo-Reductive Conditions , 2002 .

[9]  Douglas C. Elliott,et al.  Historical Developments in Hydroprocessing Bio-oils , 2007 .

[10]  J. Adjaye,et al.  Theoretical investigations of the structures and properties of molybdenum-based sulfide catalysts , 2004 .

[11]  F. Hutschka,et al.  Theoretical Study of the MoS2 (100) Surface: A Chemical Potential Analysis of Sulfur and Hydrogen Coverage , 2000 .

[12]  E. Furimsky The mechanism of catalytic hydrodeoxygenation of furan , 1983 .

[13]  A. Bridgwater,et al.  Overview of Applications of Biomass Fast Pyrolysis Oil , 2004 .

[14]  J. Nørskov,et al.  Location and coordination of promoter atoms in Co- and Ni-promoted MoS2-based hydrotreating catalysts , 2007 .

[15]  Edmond Payen,et al.  Computational studies of (mixed) sulfide hydrotreating catalysts , 2008 .

[16]  F. Maugé,et al.  CO adsorption on CoMo and NiMo sulfide catalysts: a combined IR and DFT study. , 2006, The journal of physical chemistry. B.

[17]  Edmond Payen,et al.  DFT study of thiophene adsorption on molybdenum sulfide , 2006 .

[18]  Fabrice Diehl,et al.  On the hydrodesulfurization of FCC gasoline: a review , 2005 .

[19]  F. Maugé,et al.  Towards the characterization of active phase of (Co)Mo sulfide catalysts under reaction conditions—Parallel between IR spectroscopy, HDS and HDN tests , 2007 .

[20]  A. Ishihara,et al.  Elucidation by computer simulations of the CUS regeneration mechanism during HDS over MoS2 in combination with 35S experiments , 2003 .

[21]  J. Nørskov,et al.  The effect of Co-promotion on MoS2 catalysts for hydrodesulfurization of thiophene: A density functional study , 2009 .

[22]  A. Daudin,et al.  Impact of CO on the transformation of a model FCC gasoline over CoMoS/Al2O3 catalysts: A combined kinetic and DFT approach , 2010 .

[23]  J. Paul,et al.  DFT study of furan adsorption over stable molybdenum sulfide catalyst under HDO conditions , 2009 .

[24]  P. Raybaud,et al.  Mixed sites and promoter segregation: A DFT study of the manifestation of Le Chatelier's principle for the Co(Ni)MoS active phase in reaction conditions , 2008 .

[25]  Y. Romero,et al.  Hydrodeoxygenation of benzofuran and its oxygenated derivatives (2,3-dihydrobenzofuran and 2-ethylphenol) over NiMoP/Al2O3 catalyst , 2009 .

[26]  Mingyong Sun,et al.  Adsorption and dissociation of H2 and H2S on MoS2 and NiMoS catalysts , 2005 .

[27]  I. Stensgaard,et al.  Atomic-scale structure of Co-Mo-S nanoclusters in hydrotreating catalysts , 2001 .

[28]  M. Klein,et al.  Reaction pathway analysis of thermal and catalytic lignin fragmentation by use of model compounds , 1983 .

[29]  Avelino Corma,et al.  Synergies between bio- and oil refineries for the production of fuels from biomass. , 2007, Angewandte Chemie.

[30]  A. Krause,et al.  Effect of hydrogen sulphide on the hydrodeoxygenation of aromatic and aliphatic oxygenates on sulphided catalysts , 2007 .

[31]  Jackson,et al.  Atoms, molecules, solids, and surfaces: Applications of the generalized gradient approximation for exchange and correlation. , 1992, Physical review. B, Condensed matter.

[32]  T. Zeng,et al.  Density functional theory study of CO adsorption on molybdenum sulfide. , 2005, Journal of Physical Chemistry B.

[33]  D. Hudebine,et al.  Inhibiting effect of oxygenated model compounds on the HDS of dibenzothiophenes over CoMoP/Al2O3 catalyst , 2010 .

[34]  G. Kresse,et al.  From ultrasoft pseudopotentials to the projector augmented-wave method , 1999 .

[35]  Pascal Raybaud,et al.  Understanding and predicting improved sulfide catalysts: Insights from first principles modeling , 2007 .

[36]  D. Duprez,et al.  Kinetic study of olefin hydrogenation on hydrotreating catalysts , 2010 .

[37]  Chunshan Song An overview of new approaches to deep desulfurization for ultra-clean gasoline, diesel fuel and jet fuel , 2003 .

[38]  David Loffreda,et al.  Theoretical insight of adsorption thermodynamics of multifunctional molecules on metal surfaces , 2006 .