Catalyst compositions comprising small size molecular sieves crystals deposited on a porous material

Patent metadata

Field	Value
Publication number	US-10894246-B2
Application number	US-201916269320-A
Country	US
Kind code	B2
Filing date	Feb 6, 2019
Priority date	Jul 4, 2013
Publication date	Jan 19, 2021
Grant date	Jan 19, 2021

Abstract

Catalyst compositions comprising an inorganic porous material with pore diameters of at least 2 nm and of crystals of molecular sieve, characterized in that the crystals of molecular sieve have an average diameter, measured by scanning electron microscopy, not bigger than 50 nm, and in that the catalyst composition presents a concentration of acid sites ranges from 50 to 1200 μmol/g measured by TPD NH3 adsorption; and the XRD pattern of said catalyst composition is the same as the X ray diffraction pattern of said inorganic porous material.

First claim

The invention claimed is:

1. A process of preparation of a catalyst composition comprising:
a) providing an inorganic porous material;
b) optionally calcinating the inorganic porous material at temperature from 400° C. to 1200° C.;
c) providing a solution containing at least one charge surface modifying agent selected from the group consisting of inorganic surface modifying agents, ionic or non-ionic surfactants, water soluble anionic polymers, and water soluble cationic polymers;
d) putting in contact the solution of step c) and the inorganic porous material to obtain a modified inorganic porous material modified with a charge surface modifying agent;
e) providing a solution containing precursors for a molecular sieve;
f) preparing the molecular sieves by:
i) maturating, during a period of time from of no more than 100 h, the solution of step e), the maturating process being followed by dynamic light scattering (DLS) and stopped when crystals of molecular sieve have a maximum size of 50 nm, and subjecting the modified inorganic porous material to a contact with the maturated solution to deposit molecular sieve crystals on the surface of the modified inorganic porous material obtained at step d); and/or
ii) putting in contact the modified inorganic porous material obtained at step d) with the solution of step e) and maturating during a period of time of no more than 100 h the obtained mixture until the acidity of the catalyst composition measured by TPD ammonia has increased by at least 10% compared with the acidity of the inorganic porous material;

g) separating solid from liquid if any of the mixture obtained after step f); and
h) calcinating the solid obtained at step g) to form the catalyst composition, wherein the catalyst composition comprises:
an inorganic porous material with pore diameters of at least 2 nm and crystals of molecular sieve;

wherein the crystals of molecular sieve have an average diameter not bigger than 50 nm measured using Scanning Electron Microscopy, wherein the crystals of molecular sieve comprise a zeolite selected from the group consisting of MOR, FAU, EMM, MWW, BETA, ZSM-21, ZSM-42, AEI, CHA, ERI, LEV, OFF, ZSM-34, AFI, AEL, LTL, MFI (ZSM-5, silicalite, TS-1), MEL (ZSM-11, silicalite-2, TS-2), MTT (ZSM-23, EU-13, ISI-4, KZ-1), MFS (ZSM-57), HEU (Clinoptilolite), FER (ZSM-35, Ferrierite, FU-9, ISI-6, NU-23, Sr-D), TON (ZSM-22, Theta-1, ISI-1, KZ-2 and NU-10), LTL (L), MAZ (mazzite, Omega, ZSM-4) and mixtures thereof;
wherein the catalyst composition has a concentration of acid sites ranging from 50 to 1200 μmol/g measured by Temperature-Programmed Desorption of ammonia, TPD NH3; and
wherein an X-ray diffraction pattern of the catalyst composition is the same as an X-ray diffraction pattern of the inorganic porous material.

2. The process according to claim 1 , further characterized in that the steps e) to g) are repeated at least two times prior to performing step h).

3. The process according to claim 2 , wherein the maturation of the solution is conducted for at least 30 min and at most 100 h each time.

4. The process according to claim 3 , wherein the steps e) to g) are performed once and maturation of the solution is conducted for at most 50 h.

5. The process according to claim 1 , further comprising, after step h), performing one or more of the following steps:
introducing phosphorous on to the catalyst composition by impregnation of the catalyst composition by a solution containing phosphorous, said step being optionally followed by further steps of calcinations and/or steaming;
adding at least one metal to the catalyst composition by impregnation of the catalyst composition by a solution containing the at least one metal, wherein the at least on metal is selected from the group consisting of: B, Cr, Co, Ga, Fe, Li, Mg, Ca, Mn, La, Ti, Mo, W, Ni, Ag, Sn or Zn, Pt, Pd, Ru, Re, Os, Au, and combinations thereof;
adding at least one binder selected from the group consisting of: silica, silica alumina, metal silicates, metal oxides and/or metals, amorphous alumophophate or silica alumophosphates, gels including mixtures of silica and metal oxides, and combinations thereof, by spray drying or extrusion;
shaping of the catalyst composition by extrusion.

Assignees

• Total Res & Technology Feluy
• Centre Nat Rech Scient

Inventors

• Haw Kok-Giap
• Goupil Jean-Michel
• Gilson Jean-Pierre
• VALTCHEV Valentin
• Nesterenko Nikolai
• Minoux Delphine
• Dath Jean-Pierre

Classifications

• B01J35/77

  Compounds characterised by their crystallite size · CPC title

• B01J35/45

  Nanoparticles · CPC title

• C10G47/12

  Inorganic carriers · CPC title

• C10G45/62

  containing platinum group metals or compounds thereof · CPC title

• Y02P30/20

  using bio-feedstock · CPC title