Classifications

• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
  • C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
  • C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
  • C01B39/20—Faujasite type, e.g. type X or Y
  • C01B39/205—Faujasite type, e.g. type X or Y using at least one organic template directing agent; Hexagonal faujasite; Intergrowth products of cubic and hexagonal faujasite
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J29/00—Catalysts comprising molecular sieves
  • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
  • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
  • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
  • B01J29/084—Y-type faujasite
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J35/00—Catalysts, in general, characterised by their form or physical properties
  • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
  • B01J35/61—Surface area
  • B01J35/612—Surface area less than 10 m2/g
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
  • C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
  • C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
  • C01B39/20—Faujasite type, e.g. type X or Y
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
  • C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
  • C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
  • C01B39/20—Faujasite type, e.g. type X or Y
  • C01B39/24—Type Y
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2002/00—Crystal-structural characteristics
  • C01P2002/01—Crystal-structural characteristics depicted by a TEM-image
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2002/00—Crystal-structural characteristics
  • C01P2002/30—Three-dimensional structures
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2002/00—Crystal-structural characteristics
  • C01P2002/60—Compounds characterised by their crystallite size
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2002/00—Crystal-structural characteristics
  • C01P2002/70—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
  • C01P2002/72—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data by d-values or two theta-values, e.g. as X-ray diagram

Definitions

• the present invention relates to a new process for the preparation of an FAU structural type Y zeolite whose crystal size is less than 100 nm, which is called throughout the rest of the text "nanoscale zeolite", having a Si ratio.
• Said nanometric zeolite of structural type FAU advantageously finds its application as a catalyst, adsorbent or separating agent.
• Zeolites, or molecular sieves are crystalline materials consisting of a three-dimensional arrangement of interconnected T0 4 tetrahedra (T may be Si, Al, B, P, Ge, Ti, Ga, Fe, for example).
• T may be Si, Al, B, P, Ge, Ti, Ga, Fe, for example.
• the organization of elements T0 4 generates an ordered network of micropores consisting of channels and cavities whose dimensions are compatible with small organic molecules.
• there are different zeolitic structures there are more than 220 [http: //www.iza-structure.org/databases]). Each structure therefore has a clean crystal lattice that can be identified by its X-ray diffraction pattern.
• zeolites are numerous and relate to fields such as catalysis, adsorption, ion exchange or purification.
• the use of a zeolite is conditioned by the characteristics of its porous network (dimensions, etc.) and its chemical composition.
• An aluminosilicic zeolite has a negatively charged framework, because of the charge deficit provided by each aluminum atom relative to silicon, and which therefore requires the presence of easily exchangeable compensation cations (Na + , K + , etc.).
• NH 4 + ammonium cations it is then possible to calcine the zeolite in order to obtain an acid structure (the NH 4 + are converted to H + by removal of NH 3 ).
• Such materials find applications in acid catalysis, where their activity and their selectivity will depend on the strength of the acid sites, their density and their location, as well as their accessibility.
• zeolites of structural type FAU which are used in many industrial processes such as catalytic cracking of heavy oil cuts.
• zeolite X having a Si / Al ratio of structure of between 1 and 1.5 [R.M. Milton, U.S. Patent 2,882,244, 1959] and zeolite Y for which the Si / Al ratio is greater than 1.5 [D.W. Breck, US Patent 3,130,007, 1964].
• the aO mesh parameter of faujasite can vary between 24.2 and 24.8 ⁇ according to the Si / Al framework ratio [DW Breck, EM Flanigen, Molecular Sieves, Society of Chemical Industry, London (1968) 47; JR Sohn, SJ DeCanio, JH Lunsford, DJ O'Donnell, Zeolites 6 (1986) 225; H. Fichtner-Schmittler, U. Lohse, G. Engelhardt, V. Patzelova, Cryst. Res. Technol. 19 (1984)].
• the arrangement of the tetrahedra gives rise to supercages with a maximum diameter of 1 1, 6 ⁇ and acting as nanoreactors adapted to the cracking of hydrocarbons and the adsorption of gas; Moreover, the pore of the faujasite, with a diameter of 7.4 ⁇ for 12 T04 tetrahedrons, allows a good diffusion of molecules within the porous network [C. Baerlocher, LB McCusker, DH Oison, Atlas of Zeolite Framework Type, 6th revised edition, Elsevier (2007)].
• An object of the present invention is to provide a method for preparing a zeolite Y structural type FAU and having nanoscale dimensions.
• Nano-sized zeolites have a strong catalytic interest because of their improved diffusion properties: unlike zeolites of micrometric dimensions in which the length of the intracrystalline diffusion paths causes a restriction of the catalytic performances [Y. Tao, H. Kanoh, L. Abrams, K. Kaneko, Chem. Rev. 106 (2006) 896] and progressive deactivation of the catalyst [K. Na, M. Choi, R. Ryoo, Micro. Meso. Mater. 1 66 (2013) 3], nanoscale zeolites exhibit gains in activity and selectivity [D. Karami, S. Rohani, Petroleum Science and Technology 31 (2013) 1625; Q.
• the present invention makes it possible to obtain a zeolite Y of structural type FAU and whose crystals have dimensions of less than 100 nanometers.
• An essential aspect of the preparation process according to the invention is to make it possible to obtain such a nanometric Y zeolite of structural type FAU having both a crystal size of less than 100 nm, an A / B ratio and preferably Si / AI high and in particular greater than 2, and also a very good crystallinity, compared to conventional methods of the prior art does not allow to obtain zeolite Y high ratio A / B and preferably Si / Al.
• the crystallinity is defined in the context of the present invention by a microporous volume of the zeolite determined by nitrogen adsorption, greater than 0.25 cm 3 / g, preferably greater than 0.28 cm 3 / g and very preferred greater than 0.3 cm 3 / g.
• micropores is meant pores whose opening is less than 2 nm.
• micropore volume is measured by nitrogen porosimetry.
• the quantitative analysis of the microporosity is carried out using the "t" method (Lippens-De Boer method, 1965) which corresponds to a transformation of the starting adsorption isotherm as described in the book “Adsorption by powders and porous solids. Principles, methodology and applications "written by F. Rouquérol, J. Rouquérol and K. Sing, Academy Press, 1999.
• the subject of the present invention is a process for preparing a nanometer zeolite of structural type FAU having a crystal size of less than 100 nm and an A / B ratio and preferably Si / Al of greater than 2, preferably greater than 2. , 3, preferably greater than 2.5 and very preferably greater than 2.6, said method comprising at least the following steps: i) mixing, in an aqueous medium, at least one source A0 2 of at least one tetravalent element A chosen from among silicon, germanium, titanium alone or as a mixture, of at least one source BO b of at least one trivalent element B chosen from aluminum, boron, iron, indium, gallium, alone or as a mixture, of at least one C 2 / m 2 source of an alkali or alkaline earth metal C selected from lithium, sodium, potassium, calcium, magnesium alone or in a mixture, said source C 2 / m O of alkali metal or alkaline earth C also comprising at least a hydroxide ion source for obtaining
• v is between 1 and 40, preferably between 1 and 20 and very preferably between 15 and 20,
• w being between 0.1 and 5, preferably between 0.2 and 1.5;
• x being between 1 and 40, preferably between 1 and 20
• b being between 1 and 3
• b being an integer or rational number
• m being equal to 1 or 2
• v is between 5 and 50, preferably between 10 and 35 and very preferably between 20 and 30,
• w being between 0.1 and 5, preferably between 0.2 and 1.5;
• x being between 1 and 40, preferably between 1 and 20
• b being between 1 and 3
• b being an integer or rational number
• step (iii) the hydrothermal treatment of the gel obtained at the end of step (iii) at a temperature of between 20 ° C. and 200 ° C., preferably between 40 ° C. and 140 ° C. C, preferably between 50 ° C and 100 ° C, and very preferably between 60 and 80 ° C, under autogenous reaction pressure, for a period of between 1 hour and 14 days, preferably between 6 hours and 7 hours; days, preferably between 10 hours and 3 days and very preferably between 16 hours and 24 hours, to obtain the crystallization of said nanometric zeolite Y of structural type FAU.
• the present invention therefore makes it possible to obtain a zeolite Y of structural type FAU having both a crystal size of less than 100 nm and an A / B ratio and preferably Si / Al of greater than 2 thanks to the implementation a maturing step in which is added to a source of a tetravalent element A selected from silicon, germanium, titanium, alone or in admixture.
• the process according to the invention also makes it possible to obtain zeolite crystals of structural type FAU, with a ratio A / B and preferably Si / Al greater than 2, of size less than 100 nm and whose crystallinity is improved compared with state of the art. This results in a microporous volume of the zeolite determined by nitrogen adsorption, greater than 0.25 cm 3 / g, preferably greater than 0.28 cm 3 / g and very preferably greater than 0.3 cm 3 / boy Wut.
• At least one source A0 2 of at least one tetravalent element A is incorporated in step (i) of the preparation process.
• A is chosen from silicon, germanium, titanium and the mixture of at least two of these tetravalent elements and very preferably A is silicon.
• the source (s) of the said tetravalent element (s) may be any compound comprising element A and capable of releasing this element in aqueous solution in reactive form.
• Element A is incorporated into the mixture in an oxidized form A0 2 or in any other form.
• A is titanium, Ti (EtO) 4 is advantageously used as a source of titanium.
• A is germanium, amorphous GeO 2 is advantageously used as the source of germanium.
• the silicon source may be any one of the sources commonly used for the synthesis of zeolites, for example powdered silica, silicic acid, colloidal silica, dissolved silica or tetraethoxysilane (TEOS).
• powdered silicas it is possible to use precipitated silicas, especially those obtained by precipitation from an alkali metal silicate solution, pyrogenic silicas, for example "CAB-O-SIL” and silica gels.
• Colloidal silicas having different particle sizes, for example having a mean equivalent diameter of between 10 and 15 nm or between 40 and 50 nm, such as those sold under registered trademarks such as "LUDOX” may be used.
• the silicon source is LUDOX.
• At least one source C 2 / m O of an alkali metal or alkaline earth metal C is incorporated in step (i) of the preparation process.
• C is one or more alkali metal (s) and / or alkaline earth metal (s). preferably selected from lithium, sodium, potassium, calcium, magnesium and the mixture of at least two of these metals, and most preferably C is sodium.
• the source (s) C 2 / m O (es) said (s) of an alkali metal or alkaline earth C can be any compound comprising the element C and can release this element in solution aqueous reactive form.
• said source C 2 / m O alkali metal or alkaline earth C can also release at least one source of hydroxide ions in aqueous solution.
• the C 2 / m 2 source of an alkali metal or alkaline earth metal C also comprising at least one source of hydroxide ions is chosen from lithium hydroxide, sodium hydroxide and potassium hydroxide. , calcium hydroxide and magnesium hydroxide, alone or in admixture.
• At least one source BOb of at least one trivalent element B is added in step (i) of mixing the preparation process.
• said trivalent element B is chosen from aluminum, boron, iron, indium, gallium or the mixture of at least two of these trivalent elements and very preferably B is aluminum.
• the source (s) of said trivalent element (s) B may be any compound comprising element B and capable of releasing this element in aqueous solution in reactive form.
• Element B may be incorporated into the mixture in oxidized form BO b with 1 ⁇ b ⁇ 3 (b being an integer or rational number) or in any other form.
• the aluminum source is preferably sodium aluminate or an aluminum salt, for example chloride, nitrate, hydroxide or sulphate, an alkoxide aluminum or alumina itself, preferably in hydrated or hydratable form, such as for example colloidal alumina, pseudoboehmite, gamma alumina or alpha or beta trihydrate. It is also possible to use mixtures of the sources mentioned above. According to the invention, the different sources are added in step (i) of mixing so that the reaction mixture has the following molar composition: v A0 2 : w BO b : x C 2 / m O: y H 2 0
• v is between 1 and 40, preferably between 1 and 20 and very preferably between 15 and 20,
• w being between 0.1 and 5, preferably between 0.2 and 1.5;
• x being between 1 and 40, preferably between 1 and 20
• b being between 1 and 3
• b being an integer or rational number
• A, B and C have the same definition as above, namely A is one or more tetravalent element (s) chosen from the group formed by the following elements: silicon, germanium, titanium, very preferably A is silicon, where B is one or more trivalent element (s) chosen from the group formed by the following elements: aluminum, iron, boron, indium and gallium, very preferably B is aluminum, where C is one or more alkali metal (s) and / or alkaline earth metal (s) chosen from lithium, sodium, potassium, calcium, magnesium and the mixture of at least two of these metals, very preferably C is sodium.
• said mixing step (i) is carried out in the absence of organic structuring agent.
• Step (i) of the process according to the invention consists in preparing an aqueous reaction mixture called gel containing at least one source A0 2 of at least one tetravalent element A, at least one source B b of at least one element trivalent B, B being preferably aluminum, at least one source C 2 / m O of an alkali metal or alkaline earth C, C being preferably sodium.
• the amounts of said reagents are adjusted so as to confer on this gel a composition allowing its crystallization into a nanometric Y zeolite of structural type FAU.
• Step (i) of the process of the invention may be advantageous to add seeds to the reaction mixture during said step (i) of the process of the invention in order to reduce the time required for the formation of nanometer zeolite Y crystals of structural type FAU and / or the duration total crystallization. Said seeds also promote the formation of said zeolite Y structural type FAU at the expense of impurities.
• Such seeds comprise crystalline solids, preferably zeolite crystals of structural type FAU.
• the crystalline seeds are generally added in a proportion of between 0.01 and 10% of the mass of the source of element A, preferably oxide A0 2 , used in the reaction mixture.
• Step (ii) of the process according to the invention consists in carrying out a maturation of the gel obtained at the end of step (i) of mixing.
• Said ripening step can be carried out with or without agitation, in static condition.
• said step is preferably carried out with magnetic or mechanical stirring, with a stirring speed of between 0 and 1000 rpm.
• Said ripening step advantageously operates at a temperature of between -15 ° C. and 60 ° C., preferably between 0 ° C. and 50 ° C., and very preferably between 20 ° and 40 ° C. for a period of time between 10 ° C. and 50 ° C. hours and 60 days, preferably between 10 hours and 30 days, very preferably between 1 day and 30 days, and even more preferably between 1 day and 20 days.
• step (iii) of the process according to the invention after at least 10 hours and less than 72 hours of ripening, preferably after at least 10 hours and strictly less than 72 hours, preferably after at least 12 hours and less than 48 hours and very preferably after at least 24 hours and less than 48 hours, at least one source A0 2 of at least one tetravalent element A selected from silicon, germanium, titanium, alone or as a mixture , is added to the gel obtained at the end of step (i) of mixing.
• the addition of at least said source A0 2 therefore takes place during the step ii) of maturing, at a very specific moment of said maturing step.
• the ripening therefore continues after the addition for a period of between 10 hours and 60 days, preferably between 10 hours and 30 days, very preferred between 1 day and 30 days, and even more preferably between 1 day and 20 days.
• the addition of at least one source A0 2 of at least one tetravalent element A may advantageously be repeated one or more times, with an identical or different amount. Said repeated additions may advantageously be spaced apart for a period of between 5 minutes and 1 day, and preferably between 6 and 12 hours.
• A has the same definition as above, namely A is one or more tetravalent element (s) chosen from the group formed by the following elements: silicon, germanium, titanium, and very preferably A is the silicon.
• the source (s) of the said tetravalent element (s) may be any compound comprising element A and capable of releasing this element in aqueous solution in reactive form. Element A may be incorporated into the mixture in an oxidized form A0 2 or in any other form.
• the tetravalent element A added in step (iii) of curing the process according to the invention may be identical to or different from the tetravalent element A added in step (i) of mixing and preferably identical.
• the silicon source may be any of said sources commonly used for zeolite synthesis and described in step (i) of mixing.
• no other constituent source source of the reaction mixture other than A0 2 is added in said step iii) of the process according to the invention.
• the molar composition of the gel is as follows:
• v is between 5 and 50, preferably between 10 and 35 and very preferably between 20 and 30,
• w being between 0.1 and 5, preferably between 0.2 and 1.5;
• x being between 1 and 40, preferably between 1 and 20
• n 1 or 2.
• step (iv) of the process according to the invention the gel obtained at the end of step (iii) of adding a source of at least one tetravalent element A is subjected to a hydrothermal treatment , carried out at a temperature between 20 ° C and 200 ° C, preferably between 40 ° C and 140 ° C, preferably between 50 ° C and 100 ° C, and very preferably between 60 and 80 ° C, under autogenous reaction pressure, for a period of between 1 hour and 14 days, preferably between 6 hours and 7 days, preferably between 10 hours and 3 days and very preferably between 16 hours and 24 hours to obtain crystallization of said nanometric zeolite Y of structural type FAU.
• a hydrothermal treatment carried out at a temperature between 20 ° C and 200 ° C, preferably between 40 ° C and 140 ° C, preferably between 50 ° C and 100 ° C, and very preferably between 60 and 80 ° C, under autogenous reaction pressure, for a period of between 1 hour
• Step (iv) of the preparation process according to the invention is carried out under static conditions or with stirring.
• the solid phase formed of nanoscale Y zeolite FAU structural type is advantageously filtered, washed and dried.
• the drying is preferably carried out at a temperature between 20 ° C and 150 ° C, preferably between 70 ° C and 120 ° C for a period of between 5 and 20 hours.
• the nanometric Y zeolite of structural type FAU, dried, is generally analyzed by X-ray diffraction, this technique also making it possible to determine the purity of said zeolite obtained by the process of the invention.
• the process of the invention leads to the formation of a nanometric Y zeolite of pure FAU structural type, in the absence of any other crystalline or amorphous phase.
• Said nanometric zeolite of FAU structural type, obtained at the end of step (iv) and optionally dried, is called synthetic crude zeolite.
• said synthetic crude zeolite possibly undergoes at least one calcination step and at least one exchange step ion.
• all the conventional methods known to those skilled in the art can be used.
• the calcination of the nanoscale zeolite of synthetic FAU structural type obtained by the process of the invention is preferably carried out at a temperature between 500 and 700 ° C and for a period of between 5 and 15 hours.
• the preparation process according to the invention makes it possible to obtain a Y zeolite having a crystal size of less than 100 nm, preferably less than 60 nm, and preferably less than 50 nm and an A / B ratio, and preferably If / Al greater than 2, preferably greater than 2.3, more preferably greater than 2.5 and most preferably greater than 2.6.
• the size of the crystals of the zeolite obtained is measured on one or more transmission electron micrographs; this is the maximum size observed on the snapshots.
• the cation (s) C of the nanometric Y zeolite of FAU structural type obtained by the process of the invention may be replaced by one or more cation (s) of metals and in particular those of groups IA, IB, MA, MB, NIA, IIIB (including rare earths), VIII (including noble metals) as well as lead, tin and bismuth by a step ion exchange.
• Said ion exchange step is carried out by means of any water-soluble salts containing the appropriate cation.
• the hydrogen form of the nanometric zeolite Y of structural type FAU obtained by the preparation method according to the invention can be obtained by carrying out an ion exchange with an acid, in particular a strong mineral acid such as hydrochloric, sulfuric or nitric acid, or with a compound such as ammonium chloride, sulphate or nitrate .
• Said ion exchange step may advantageously be carried out by suspending said nanometric Y zeolite of structural type FAU in one or more times with the ion exchange solution.
• Said zeolite can be calcined before or after the ion exchange step, or between two ion exchange steps. Calcination of said zeolite after the ion exchange step or steps makes it possible to obtain the acid form thereof.
• Said acid form of the nanoscale zeolite can advantageously be used for applications in catalysis.
• Said zeolite Y of structural type FAU obtained by the process according to the invention advantageously has an X-ray diffraction pattern including at least the lines listed in the table corresponding to the X-ray diffraction diagram of the zeolite below:
• the relative intensity l / 10 is given in relation to a relative intensity scale where a value of 100 is assigned to the most intense line of the X-ray diffraction pattern: ff ⁇ 15; ⁇ F ⁇ 30; ⁇ Mf ⁇ 50; 50 ⁇ m ⁇ 65; 65 ⁇ F ⁇ 85;FF> 85.
• the zeolite obtained by the process of the invention can be used after ion exchange as an acid solid for catalysis, that is to say as a catalyst in the fields of refining and petrochemistry. It can also be used as an adsorbent for pollution control or as a molecular sieve for separation.
• the zeolite prepared according to the process of the invention is calcined, exchanged and is preferably in hydrogen form, and may be combined with an inorganic matrix, which may be inert or catalytically active. , and a metallic phase.
• the inorganic matrix can be present simply as a binder to hold small particles of the zeolite together in the various known forms of catalysts (extrudates, pellets, beads, powders), or can be added as a diluent to impose the degree of conversion in a a process which would progress if not at a rate too fast leading to a clogging of the catalyst as a result of a significant formation of coke.
• Typical inorganic matrices are in particular support materials for catalysts such as silica, the various forms of alumina, magnesia, zirconia, oxides of titanium, boron, zirconium, aluminum phosphates, titanium, kaolinic clays, bentonites, montmorillonites, sepiolite, attapulgite, fuller's earth, synthetic porous materials such as Si0 2 -Al 2 0 3 , Si0 2 -Zr0 2 , Si0 2 -Th0 2 , Si0 2 - BeO, Si0 2 -Ti0 2 or any combination of these compounds.
• the inorganic matrix may be a mixture of different compounds, in particular an inert phase and an active phase.
• the zeolite prepared according to the method of the invention may also be associated with at least one other zeolite and act as the main active phase or additive.
• the metal phase is introduced on the zeolite alone, the inorganic matrix alone or the inorganic-zeolite matrix assembly by ion exchange or impregnation with cations or oxides selected from the following elements: Cu, Ag, Ga, Mg, Ca, Sr, Zn, Cd, B, Al, Sn, Pb, V, P, Sb, Cr, Mo, W, Mn, Re, Fe, Co, Ni, Pt, Pd, Ru, Rh, Os, Ir and any other element of the periodic table of elements.
• the metals can be introduced either all in the same way, or by different techniques, at any time of the preparation, before or after shaping and in any order.
• intermediate treatments such as for example calcination and / or reduction can be applied between the deposits of different metals.
• the catalytic compositions comprising the nanometric zeolite Y of FAU structural type prepared according to the process of the invention are generally suitable for the implementation of the main hydrocarbon conversion processes and the synthesis reactions of organic compounds such as ethers. .
• any shaping method known to those skilled in the art is suitable for the catalyst comprising zeolite Y nanometric structural type FAU. It is possible to use, for example, pelletizing or extruding or forming beads.
• the shaping of the catalyst containing the zeolite prepared by the process of the invention and at least partly in acid form is generally such that the catalyst is preferably in the form of extrudates or beads for use.
• FIG. 4 represents the dinitrogen adsorption-desorption isotherm of the FAU structural type zeolite Y synthesized in example 3 according to the invention.
• EXAMPLE 1 Preparation of a nanometric zeolite X of structural type FAU and of molar ratio Si / Al equal to 1, 4 according to a process not according to the invention in that no source of silicon or any other tetravalent element is added during the ripening step.
• a nanometric X-zeolite of FAU structural type containing the elements Si and Al, with a molar ratio Si / Al equal to 1.4, is synthesized according to a method of preparation known to those skilled in the art.
• the source of aluminum sodium aluminate, Strem Chemicals, 99%
• the mineralizing agent sodium hydroxide, Fluka, 99%
• the silicon source (Ludox AS-40, 40%, Sigma Aldrich) is then added dropwise, in order to obtain a reaction mixture whose molar composition is 15.2 SiO 2 : 1 Al 2 O 3 : Na 2 O: 360H 2 O.
• the reaction mixture is stirred vigorously for 17 days at room temperature.
• the product is then filtered and washed, before being dried in an oven overnight at 100 ° C. No source of silicon or any other tetravalent element is added during the curing step.
• the X-ray diffraction pattern of the material shown in FIG. 1 is indexable in the cubic system of the FAU structural type zeolite.
• the analysis of the X-ray diffractogram gives a molar ratio Si / Al equal to 1, according to the Fichtner-Schmittler equation. These characteristics correspond to a zeolite X of structural type FAU.
• the size of the crystals of the zeolite obtained, measured on 8 transmission electron micrographs, is between 15 and 50 nm.
• a nanometric Y zeolite of FAU structural type containing the elements Si and Al, with a Si / Al molar ratio equal to 2.7, is synthesized according to a method of preparation described in Example 1 with regard to step (i) of mixed.
• the source of aluminum sodium aluminate, Strem Chemicals, 99%
• the mineralizing agent sodium hydroxide, Fluka, 99%
• the silicon source Lidox AS-40, 40%, Sigma Aldrich
• the gel thus formed is stirred vigorously at room temperature. After 7 days of maturing, a source of silicon (Ludox AS-40, 40%, Sigma Aldrich) is added dropwise. The operation is repeated the next day and the day after tomorrow. After the 3 silicon source additions, the gel thus formed has the following composition: SiO 2 : 1 Al 2 O 3 : 18.4 Na 2 O: 480H 2 O.
• the reaction mixture is stirred vigorously for 4 hours. additional days at room temperature and then transferred to a polypropylene vial. This bottle is placed in an oven at 60 ° C for 24 hours under autogenous pressure and without addition of gas. After cooling the flask to room temperature, the product is filtered and washed, before being dried in an oven overnight at 100 ° C.
• the X-ray diffraction pattern of the material shown in FIG. 2 is indexable in the cubic system of the FAU structural type zeolite.
• the analysis of the X-ray diffractogram gives an Si / Al molar ratio equal to 2.7 according to the Fichtner-Schmittler equation. These characteristics also correspond to a zeolite Y of structural type FAU.
• the size of the crystals of the zeolite obtained, measured on 8 transmission electron micrographs, is between 15 and 50 nm.
• the microporous volume of zeolite Y obtained according to Example 2 determined by nitrogen adsorption is equal to 0.24 cm 3 / g.
• EXAMPLE 3 Preparation of the nanometric Y zeolite of FAU structural type and of Si / Al molar ratio equal to 2.4 according to a method according to the invention in that the addition of a silicon source is carried out after 1 day of maturation.
• a nanometric Y zeolite of structural type FAU containing the elements Si and Al, with a molar ratio Si / Al equal to 2.4, is synthesized according to the following method of preparation.
• the source of aluminum (sodium aluminate, Sigma Aldrich, 53% Al 2 O 3 , 43% Na 2 O, 4% H 2 O) and the mineralizing agent (sodium hydroxide, Carlo Erba, 99%) are dissolved in deionized water, with stirring.
• the silicon source Lidox AS-40, 40%, Sigma Aldrich
• the gel thus formed is stirred at room temperature. After 1 day of maturation, a source of silicon (Aerosil 130V, Evonik,> 99.8%) is added. After this silicon source addition, the gel thus formed has the following composition: SiO 2 : 1 Al 2 O 3 : 17 Na 2 O: 360H 2 O.
• the reaction mixture is stirred for a further 6 days at room temperature. then transferred to a polypropylene bottle. This flask is placed in an oven at 70 ° C. for 16 hours under autogenous pressure and without addition of gas. After cooling the flask to room temperature, the product is washed by centrifugation, before being dried in an oven overnight at 100 ° C.
• the X-ray diffractogram of the material shown in FIG. 1 is indexable in the cubic system of the zeolite of structural type FAU.
• the analysis of the X-ray diffractogram gives a molar ratio Si / Al equal to 2.4, according to the Breck and Flanigen equation.
• the average crystal size of the zeolite obtained, measured by transmission electron microscopy considering a total of 100 particles is about 90 nm.
• the Y zeolite obtained according to Example 3 according to the invention has a very good crystallinity. Indeed, the adsorption-desorption isotherm of dinitrogen represented in FIG. 2 makes it possible to deduce that the microporous volume of the zeolite is equal to 0.34 cm 3 / g.
• Example 4 not in accordance with the invention.
• a gel of the same composition as that described in Example 3 is prepared after the addition of a source of silicon: 36 SiO 2 : 1 Al 2 0 3 : 17 Na 2 O: 360 H 2 0.
• This gel is stirred at room temperature for 7 days, corresponding to the total maturation time of the gel prepared in Example 3.
• the reaction mixture is then transferred to a flask. made of polypropylene. This flask is placed in an oven at 70 ° C. for 16 hours under autogenous pressure and without addition of gas. After cooling the flask to room temperature, the product is washed by centrifugation, before being dried in an oven overnight at 100 ° C.
• the X-ray diffractogram of the material obtained shows that no crystallized product was formed at the end of the crystallization step at 70 ° C.
• the preparation method described in this example does not therefore make it possible to obtain a nanometric zeolite of structural type FAU.

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