Ifp Energies Nouvelles

Institut Francais Du Pe'trole

Centre National De La Recherche Scientifique

Eni S.p.a.

Institute Francais Du Petrole

Cnrs

Université De Poitiers

Iep Energies Nouvelles

Ifp Emergies Nouvelles

Universite Claude Bernard – Lyon1

Emmanuelle Guillon

Eric Sanchez

Christophe Bouchy

Amandine Cabiac

Laurent Simon

Sylvie Lacombe

Johan Adriaan Martens

Nicolas Cadran

Antoine Fecant

Nicolas Bats

Antoine Daudin

Nadine Essayem

Catherine Pinel

Franck Rataboul

Eric Benazzi

Patrick Euzen

Sylvie Maury

Magalie Roy-Auberger

Anne-Claire Dubreuil

Patrick Bourges

Thierry Chapus

Laurent Bournay

Damien Delcroix

Audrey Bonduelle

Christophe Vallee

Loic Rouleau

Natacha Touchais

Nathalie Dupassieux

Joël Patarin

Vincent Coupard

Malika Boualleg

Helene Olivier-Bourbigou

Patrick Briot

Florent Guillou

Lionel Magna

Avelino Corma

Gil Mabilon

Vincent Lecocq

Jan Verstraete

Thomas Plennevaux

Sophie Couderc

Flora Chambon

Vicente Fornes

Eva Barea

Laure Brandhorst

Simone Goergen

Gaëlle Hastoy

Aline Grezaud

Elodie Tellier

Gerhard Pirngruber

Anne Claire Pierron

Audrey Bonduelle-Skrzypczak

Ludovic Pinard

Nicolas Bais

José Manuel Serra Alfaro

Filipe Manuel Marques Mota

Ngi Suor Gnep

José Manuel Serra

Jeremy Francis

Christophe Pichon

Nuno Miguel Rocha Batalha

Francisco Manuel Da Silva Lemos

Fernando Manuel Ramoa Ribeiro

Antoíne Daudin

Pierre Moreau

Patrick Magnoux

Erie Sanchez

Johan Mariens

Philippe Rocher

Johan Martens

Anne-Claire Pierron

Nadine Essayen

Simon Laurent

Gaelle Hastoy

Vincent Lecoq

Vincent Fornes

Yohan Martens

The present invention is based on the use of a two-step hydrocracking process for the production of naphtha, comprising a step of hydrogenation placed downstream of the second hydrocracking step, the hydrogenation step treating the effluent resulting from the second hydrocracking step in the presence of a specific hydrogenation catalyst. Furthermore, the hydrogenation step and the second hydrocracking step are performed under specific operating conditions and in particular under quite specific temperature conditions.

Two-stage hydrocracking process for producing naphtha, comprising a hydrogenation stage implemented downstream of the second hydrocracking stage

The present invention is based on the use of a two-step hydrocracking process comprising a step of hydrogenation placed upstream of the second hydrocracking step, the hydrogenation step treating the unconverted liquid fraction separated in the distillation step in the presence of a specific hydrogenation catalyst. Furthermore, the hydrogenation step and second hydrocracking step are carried out under specific operating conditions and in particular under very specific temperature conditions.

Two-stage hydrocracking process comprising a hydrogenation stage upstream of the second hydrocracking stage, for the production of middle distillates

The present invention is based on the use of a two-step hydrocracking process for the production of naphtha, comprising a step of hydrogenation placed upstream of the second hydrocracking step, the hydrogenation step treating the unconverted liquid fraction separated in the distillation step in the presence of a specific hydrogenation catalyst. Furthermore, the hydrogenation step and a second hydrocracking step are carried out under specific operating conditions and in particular under temperature conditions that are very specific with respect to one another.

Two-step hydrocracking process for the production of naphtha comprising a hydrogenation step carried out upstream of the second hydrocracking step

The invention concerns a catalyst comprising at least one zeolite with structure type MTW, a matrix, at least one metal from group VIII of the periodic classification of the elements, said catalyst having a mesopore volume increased by at least 10% compared with its initial mesopore volume, which is generally in the range 0.55 to 0.75 mL/g, at the end of a treatment with steam at a partial pressure in the range 0.01 to 0.07 MPa and at a temperature in the range 300&#xb0; C. to 400&#xb0; C. for at least 0.5 hour. The invention concerns the process for the preparation of said catalyst as well as an isomerization process employing said catalyst.

Modified catalyst with structure type MTW, a method for its preparation and its use in a process for the isomerization of an aromatic C8 cut

A process for hydrocracking hydrocarbon-containing VD feedstocks allowing the improved production of middle distillates: a) hydrocracking of feedstocks in hydrogen and at least one hydrocracking catalyst, b) gas/liquid separation of effluent originating from a) producing a liquid effluent and a gaseous effluent with hydrogen, c) comprising the gaseous effluent before recycling into hydrocracking a), d) fractionation of liquid effluent into at least one effluent of converted hydrocarbon-containing products having boiling points less than 340&#xb0; C. and an unconverted liquid fraction having a boiling point greater than 340&#xb0; C., e) hydrocracking unconverted liquid fraction from d), in hydrogen and a hydrocracking catalyst, f) hydrotreating effluent from e) in a mixture with a hydrocarbon-containing gas-oil liquid feedstock having at least 95% by weight of compounds boiling at a boiling point between 150 and 400&#xb0; C., hydrotreating f) operating in hydrogen and with at least one hydrotreating catalyst.

Process integrating two-stage hydrocracking and a hydrotreatment process

The present invention describes a process for hydrocracking at least one hydrocarbon feed in which at least 50% by weight of the compounds have an initial boiling point of more than 300&#xb0; C. and a final boiling point of less than 540&#xb0; C. using at least one catalyst comprising at least one metal from group VIB and/or at least one metal from group VIII of the periodic classification of the elements and a support comprising at least one zeolite containing at least one series of channels the opening of which is defined by a ring containing 12 oxygen atoms (12MR), and at least one binder, said support being prepared from a highly dispersible alumina gel, said hydrocracking process being operated at a temperature in the range 200&#xb0; C. to 480&#xb0; C., at a total pressure in the range 1 MPa to 25 MPa, with a ratio of the volume of hydrogen to the volume of hydrocarbon feed in the range 80 to 5000 litres per litre and with an hourly space velocity (HSV), defined as the ratio of the volume flow rate of liquid hydrocarbon feed to the volume of catalyst charged into the reactor, in the range 0.1 to 50 h.

Method for hydrocracking hydrocarbon feedstocks using a catalyst comprising a zeolite and an amorphous mesoporous alumina

The invention concerns a process for the transformation of lignocellulosic biomass or cellulose into mono- or poly-oxygenated compounds, in which the lignocellulosic biomass or the cellulose is brought into simultaneous contact with a catalytic system comprising a combination of one or more homogeneous catalysts and one or more heterogeneous catalysts, in the same reaction chamber, in the presence of at least one solvent, said solvent being water alone or as a mixture with at least one other solvent, in a reducing atmosphere, and at a temperature in the range 80&#xb0; C. to 250&#xb0; C. and at a pressure in the range 0.5 MPa to 20 MPa.

Process for the transformation of lignocellulosic biomass into mono- or poly-oxygenated molecules

The invention relates to a method of preparing a catalyst comprising a) preparation of a support comprising 0.2 to 30 wt % of zeolite NU-86 and from 70 to 99.8 wt % of a porous mineral matrix, the percentages by weight being expressed relative to the total weight of said support, b) impregnation of the support prepared according to step a) with at least one solution containing at least one precursor of at least one metal selected from group VIII metals and group VIB metals, used alone or as a mixture, c) at least one ripening step, and d) at least one drying step carried out at a temperature below 150&#xb0; C., without a subsequent calcining step. The present invention also relates to a process for hydrocracking hydrocarbon feeds using the catalyst prepared according to the method of preparation according to the invention.

Method of preparing a catalyst usable in hydroconversion comprising at least one zeolite NU-86

Process for hydrocracking and/or hydrotreatment of hydrocarbon feeds utilizing a catalyst comprising at least one hydro-dehydrogenating element of group VIB and of non-precious group VIII used alone or mixed, and a support comprising at least one porous mineral matrix and at least one dealuminated USY zeolite having an overall silicon-to-aluminium atomic ratio comprised between 2.5 and 10, a fraction by weight of extra-network aluminium atom greater than 10% relative to the total mass of the aluminium present in the zeolite, a mesopore volume measured by nitrogen porosimetry greater than 0.07 ml.g, and a crystal parameter aof the elemental mesh greater than 24.28 &#x212b;, in which a quantity of the element nickel comprised between 0.5 and 3% by weight relative to the total mass of the zeolite is deposited on said USY zeolite and in which said catalyst is in the sulphide form.

Hydrocracking process using a zeolite catalyst containing two distinct hydrogenating functions

A process for isomerizing an aromatic cut containing at least one aromatic compound containing eight carbon atoms per molecule is described, comprising bringing said cut into contact with at least one catalyst comprising at least one metal from group VIII of the periodic classification of the elements, at least one zeolitic support comprising a zeolite selected from zeolites with structure type EUO and MOR, used alone or as a mixture, and at least one matrix, such that the specific surface area of the matrix in the zeolitic support of said catalyst is in the range 5 to 200 m/g.

Method for isomerizing an aromatic C8 fraction in the presence of a catalyst containing an EUO zeolite and a specific binder

The invention relates to a catalyst comprising at least one metal selected from the group formed by metals of group VIB and of group VIII of the periodic table, used alone or as a mixture, and a support comprising at least one zeolite NU-86, at least one zeolite Y and at least one porous mineral matrix containing at least aluminum and/or at least silicon. The invention also relates to a process for hydrocracking of hydrocarbon feeds employing said catalyst.

Catalyst comprising at least one zeolite NU-86, at least one zeolite USY and a porous mineral matrix and process for hydroconversion of hydrocarbon feeds using said catalyst

A process for the hydrotreatment of a vacuum distillate type hydrocarbon feed containing nitrogen-containing compounds is described, comprising a first step in which the feed is brought into contact with a catalyst in its oxide form, then a second step in which the feed is brought into contact with a dried catalyst comprising at least one organic compound containing oxygen and/or nitrogen.

Vacuum distillate hydrotreatment process employing a concatenation of catalysts

The invention relates to a process for transformation of lignocellulosic biomass or cellulose using in a simultaneous manner an original combination of at least two homogeneous catalysts and one or more heterogeneous catalyst(s). The use of these catalysts makes it possible to obtain mono-oxidized or poly-oxidized upgradable products directly and to limit the formation of non-upgradable products. Non-upgradable products are defined as soluble and non-soluble humins, i.e., products of high molecular weight obtained from undesirable condensation reactions of sugars and their derivatives.

Method for the conversion of lignocellulosic biomasses into mono-oxygenated or poly-oxygenated molecules

The invention relates to a process for producing middle distillates from a paraffinic feedstock produced by Fischer-Tropsch synthesis, implementing a hydrocracking/hydroisomerization catalyst comprising at least one hydro-dehydrogenating metal selected from the group formed by the metals from group VIB and from group VIII of the periodic table and a substrate comprising at least one crystallized IZM-2 solid having a chemical composition, expressed on an anhydrous base, in terms of oxide moles, by the following general formula: XO:aYO:bMO, wherein X represents at least one tetravalent element, Y represents at least one trivalent element and M is at least one alkali metal and/or an alkaline earth metal of valency n, a and b representing respectively the number of moles of YOand MO and a is between 0 and 0.5 and b is between 0 and 1.

Process for producing middle distillates by hydrocracking of feedstocks obtained by the fischer-tropsch process in the presence of a catalyst comprising an IZM-2 solid

A process for isomerizing an aromatic cut containing at least one aromatic compound containing eight carbon atoms per molecule, which includes bringing the aromatic cut into contact with a catalyst containing a zeolite with structure type EUO, which catalyst has been prepared by obtaining a zeolite with structure type EUO having an overall Si/Al atomic ratio in the range 5 to 45, a sodium content in the range 500 to 5000 ppm by weight, with a Na/Al ratio in the range 5% to 20% by mole, and thereafter performing the following:

Process for isomerizing an aromatic C8 cut in the presence of a catalyst based on an euo zeolite and a particular sodium content

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Vernaison, France

Emmanuelle Guillon