Production of pulverulent, porous crystalline metal silicates by means of flame spray pyrolysis

Patent metadata

Field	Value
Publication number	US-11192794-B2
Application number	US-201816770593-A
Country	US
Kind code	B2
Filing date	Nov 23, 2018
Priority date	Dec 7, 2017
Publication date	Dec 7, 2021
Grant date	Dec 7, 2021

Abstract

The present invention relates to a process for preparing a pulverulent, porous crystalline metal silicate, comprising the following steps:a) hydrothermal synthesis in an aqueous mixture comprising (A) at least one silicon source, (B) at least one metal source and (C) at least one mineralizer to obtain an aqueous suspension comprising a porous crystalline metal silicate as reaction product; andb) calcination of the reaction product, characterized in that the calcination is conducted by means of flame spray pyrolysis at an adiabatic combustion temperature within a range of 450-2200° C., wherein the suspension having a solids content of 70% by weight which is obtained in step a) is sprayed into a flame generated by combustion of a fuel in the presence of oxygen to form a pulverulent, porous crystalline metal silicate.

First claim

The invention claimed is:

1. A process for preparing a pulverulent, porous crystalline metal silicate, comprising the steps of:
a) hydrothermal synthesis in an aqueous mixture comprising: (A) at least one silicon source; (B) at least one metal source; and (C) at least one mineralizer; to obtain an aqueous suspension comprising a porous crystalline metal silicate as a reaction product and having a solids content of ≤70% by weight; and
b) calcination of the reaction product, wherein the calcination is conducted by means of flame spray pyrolysis at an adiabatic combustion temperature within a range of 450-2200° C., wherein the suspension having a solids content of ≤70% by weight which is obtained in step a) is sprayed into a flame generated by combustion of a fuel in the presence of oxygen to form a pulverulent, porous crystalline metal silicate.

2. The process of claim 1 , wherein the porous crystalline metal silicate has a zeolite structure.

3. The process of claim 1 , wherein the porous crystalline metal silicate has a zeolite structure having a crystal structure of the LTA, MFI, FAU, MOR, MEL or MWW type.

4. The process of claim 3 , wherein the metal source is a source of elements selected from the group consisting of titanium (Ti), aluminium (Al), zirconium (Zr), iron (Fe), tin (Sn), germanium (Ge), indium (In) and boron (B).

5. The process of claim 4 , wherein the fuel is selected from the group consisting of:
hydrogen; methane; ethane, propane; butane, natural gas; and mixtures thereof.

6. The process of claim 4 , wherein the aqueous mixture in step a) additionally comprises a template selected from the group consisting of amines, quaternary ammonium compounds, alcohols and mixtures thereof.

7. The process of claim 4 , wherein, in step a), component (A) and component (B) are present together in one substance and this substance is selected from the group consisting of: amorphous mixed metal-silicon oxide, amorphous silicon dioxide doped with metal oxide, amorphous silicon dioxide impregnated with metal, metal silicate, metal-doped tetraalkyl orthosilicate and mixtures thereof.

8. The process of claim 4 , wherein step b) is followed by a shaping c) comprising the steps of:
(a) adding water to obtain an aqueous suspension of the pulverulent, porous crystalline metal silicate;
(b) mixing the suspension from step (a) with granulating aids;
(c) compacting, granulating, spray-drying, spray granulating or extruding to obtain a porous crystalline metal silicate in the form of microgranules, spheres, tablets, solid cylinders, hollow cylinders or honeycombs.

9. The process of claim 1 , wherein the fuel is selected from the group consisting of:
hydrogen, methane, ethane, propane, butane, natural gas and mixtures thereof.

10. The process of claim 1 , wherein the mean residence time of the suspension obtained in step a) in the conversion thereof in step b) is within a range from 0.1 to 10 s.

11. The process of claim 1 , wherein the ignition loss according to DIN 18128:2002-12 of the porous crystalline metal silicate is less than 5% by weight.

12. The process of claim 1 , wherein the aqueous mixture in step a) additionally comprises suitable seed crystals.

13. The process of claim 1 , wherein the aqueous mixture in step a) additionally comprises a template selected from the group consisting of amines, quaternary ammonium compounds, alcohols and mixtures thereof.

14. The process of claim 1 , wherein step a) is conducted at a temperature of 100 to 250° C. under the autogenous pressure generated in a pressure-resistant reactor.

15. The process of claim 1 , wherein, in step a), component (A) and component (B) are present together in one substance and this substance is selected from the group consisting of: amorphous mixed metal-silicon oxide; amorphous silicon dioxide doped with metal oxide; amorphous silicon dioxide impregnated with metal; metal silicate; metal-doped tetraalkyl orthosilicate; and mixtures thereof.

16. The process of claim 15 , wherein component (A) is an amorphous silicon dioxide doped with metal oxide, an amorphous silicon dioxide impregnated with metal, or an amorphous mixed metal-silicon oxide.

17. The process of claim 1 , wherein, in step a), component (A) is in solid form and component (B) is in liquid form.

18. The process of claim 17 , wherein component (A) is selected from the group consisting of: pyrogenic silicon dioxide; precipitated silicon dioxide; silicon dioxide produced by a sol-gel process; and mixtures thereof.

19. The process of claim 18 , wherein component (A) is a high-purity silicon dioxide prepared by precipitation or a pyrogenic silicon dioxide.

20. The process of claim 1 , wherein step b) is followed by a shaping c) comprising the steps of:
(a) adding water to obtain an aqueous suspension of the pulverulent, porous crystalline metal silicate;
(b) mixing the suspension from step (a) with granulating aids;
(c) compacting, granulating, spray-drying, spray granulating or extruding to obtain a porous crystalline metal silicate in the form of microgranules, spheres, tablets, solid cylinders, hollow cylinders or honeycombs.

Assignees

• Evonik Operations Gmbh

Inventors

• Schmidt Franz
• Anton Johan
• Pascaly Matthias
• Heinroth Andrea
• Wieland Stefan
• Morell Heiko
• Kress Peter
• Hagemann Michael

Classifications

• C01B39/20

  Faujasite type, e.g. type X or Y · CPC title

• 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 · CPC title

• C01B39/026 Primary

  After-treatment · CPC title

• C01B39/46

  Other types characterised by their X-ray diffraction pattern and their defined composition {(C01B39/023, C01B39/026, C01B39/06 take precedence)} · CPC title

• C01B39/38

  Type ZSM-5 · CPC title