Institut Francais Du Pe'trole

Herve Cauffriez

Eric Benazzi

Christine Travers

Jean-Francois Joly

Jean-Louis Guth

Nicolas Chouteau

The invention concerns a NU-86 zeolite comprising silicon and at least one element T selected from the group formed by aluminium, iron, gallium and boron, preferably aluminium, characterized in that element T has been extracted from the framework, and in that it has a global Si/T atomic ratio of more than about 20. Element T is extracted from the zeolitic framework (or network) by means of at least one heat treatment, optionally carried out in the presence of steam, followed by at least one acid attack using at least one solution of a mineral or organic acid, or by direct acid attack. The invention also concerns a catalyst comprising the zeolite which is at least partially in its acid form, and the use of the catalyst for the conversion of hydrocarbons, in particular for the oligomerization of olefins.

Dealuminated NU-86 zeolite and its use for the conversion of hydrocarbons

The invention concerns a catalyst composed of at least one halogen, at least one metal from group VIII and a formed support of gamma alumina and optionally eta alumina, the catalyst being characterized in that the smallest average dimension of said support is in the range 0.8 mm to 2 mm and in that the halogen content is in the range 4.5% to 15% by weight. The invention also concerns the preparation of said catalyst, preferably with chlorination (in the case where the halogen is chlorine) in the presence of CCl.sub.4 or CHCl.sub.3. The invention also concerns the use of the catalyst for the isomerisation of normal C.sub.4 -C.sub.6 paraffins.

Catalyst based on a halogenated alumina, its preparation and use for the

The present invention relates to the use of a catalyst comprising a Y zeolite with a faujasite structure combined with a NU-86 zeolite which is dealuminated and at least partially in its acid form and a matrix which is normally amorphous or of low crystallinity in a process for catalytic cracking of petroleum feeds.

Process for cracking hydrocarbon feeds using a catalyst comprising a

The present invention relates to the use of a catalyst comprising an IM-5 zeolite which has optionally been dealuminated and is at least partially in its acid form and a matrix which is normally amorphous or of low crystallinity, and optionally a Y zeolite with a faujasite structure, in a process for catalytic cracking of petroleum feeds.

Process for cracking hydrocarbon feeds using a catalyst comprising an

The present invention relates to a dealuminated IM-5 zeolite and to any catalyst comprising that zeolite which is at least partially in its acid form. The invention also relates to the preparation of the catalyst and to the catalyst. Finally, the invention relates to the use of the zeolite in a hydrocarbon conversion process.

Dealuminated IM-5 zeolite

A process for preparing aluminophosphate compounds (and substituted derivatives) of the structural type VFI. This preparation process is characterized in that the speed of increase in temperature of the reaction mixture is greater than 250.degree. C./hour, the total time of heating of the reaction mixture, including the rise in temperature and the plateau heating, being less than one hour. The temperature of the plateau heating is between 100.degree. and 200.degree. C. The synthetic compounds in accordance with the invention possess

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Bougival, France

Herve Cauffriez