Process for preparing a titanium-containing zeolitic material having an MWW framework structure

Patent metadata

Field	Value
Publication number	US-10029244-B2
Application number	US-201414764354-A
Country	US
Kind code	B2
Filing date	Feb 5, 2014
Priority date	Feb 5, 2013
Publication date	Jul 24, 2018
Grant date	Jul 24, 2018

Abstract

A process for the preparation of a titanium-containing zeolitic material having an MWW framework structure, the process comprising (i) providing a zeolitic material having an MWW framework structure comprising SiO2 and B2O3, (ii) incorporating titanium into the zeolitic material provided in (i) comprising (ii.I) preparing an aqueous synthesis mixture containing the zeolitic material provided in (i), an MWW template compound and a titanium source, (ii.2) hydrothermally synthesizing a titanium-containing zeolitic material having an MWW framework structure from the aqueous synthesis mixture prepared in (ii.1), obtaining a mother liquor comprising the titanium-containing zeolitic material having an MWW framework structure; (iii) spray-drying the mother liquor obtained from (ii.2) comprising the titanium-containing zeolitic material having an MWW framework structure.

First claim

The invention claimed is:

1. A process for preparing a titanium-comprising zeolitic material having an MWW framework structure comprising
(i) providing a zeolitic material having an MWW framework structure comprising SiO 2 and B 2 O 3 , wherein a molar ratio B 2 O 3 :SiO 2 is at most 0.02:1 and wherein at least 99 weight-% of the MWW framework structure consist of B 2 O 3 and SiO 2 ;
(ii) incorporating titanium into the zeolitic material provided in (i) comprising
(ii.1) preparing an aqueous synthesis mixture comprising the zeolitic material provided in (i), an MWW template compound and a titanium source, wherein a molar ratio of the MWW template compound relative to Si, calculated as SiO 2 and comprised in the zeolitic material provided in (i), is in a range of from 0.5:1 to 1.4:1;
(ii.2) hydrothermally synthesizing a titanium-comprising zeolitic material having an MWW framework structure from the aqueous synthesis mixture prepared in (ii.1), obtaining a mother liquor comprising the titanium-comprising zeolitic material having an MWW framework structure;

(iii) spray-drying the mother liquor obtained from (ii. 2 ) comprising the titanium-comprising zeolitic material having an MWW framework structure to obtain a spray-dried titanium-comprising zeolitic material having an MWW framework structure.

2. The process of claim 1 , wherein in (i), the zeolitic material having an MWW framework structure is provided by a process comprising
(a) hydrothermally synthesizing a B-MWW precursor comprising SiO 2 and B 2 O 3 with a molar ratio B 2 O 3 :SiO 2 of greater than 0.02:1 from a synthesis mixture comprising a silicon source, a boron source, and an MWW template compound, obtaining the B-MWW precursor in a mother liquor;
(b) separating the B-MWW precursor from the mother liquor to obtain a separated B-MWW precursor, and calcining the separated B-MWW precursor, obtaining a B-MWW;
(c) deboronating the B-MWW obtained from (b) by treating the B-MWW with a liquid solvent system obtaining the zeolitic material having an MWW framework structure and a molar ratio B 2 O 3 :SiO 2 of at most 0.02:1, and at least partially separating the zeolitic material from the liquid solvent system.

3. The process of claim 2 , wherein (c) comprises drying the zeolitic material having an MWW framework structure and a molar ratio B 2 O 3 :SiO 2 of at most 0.02:1.

4. The process of claim 2 , wherein the separated zeolitic material having an MWW framework structure and a molar ratio B 2 O 3 :SiO 2 of at most 0.02:1 obtained from (c) is not subjected to calcination prior to (ii).

5. The process of claim 2 , wherein in (c), the zeolitic material having an MWW framework structure and a molar ratio B 2 O 3 :SiO 2 of at most 0.02:1 is obtained in a form of particles having a Dv10 value in a range of from 1 to 10 micrometer, a Dv50 value in a range of from 5 to 50 micrometer, and a Dv90 value in a range of from 12 to 200 micrometer.

6. The process of claim 1 , wherein the molar ratio B 2 O 3 :SiO 2 of the zeolitic material having an MWW framework structure provided in (i) is at most 0.01:1, wherein at least 99.5 weight-% of the MWW framework structure consist of B 2 O 3 and SiO 2 .

7. The process of claim 1 , wherein in (ii.1), the MWW template compound is selected from the group consisting of piperidine, hexamethylene imine, N,N,N,N′,N′,N′-hexamethyl-1,5-pentanediammonium ion, 1,4-bis(N-methylpyrrolidinium)butane, octyltrimethylammonium hydroxide, heptyltrimethylammonium hydroxide, hexyltrimethylammonium hydroxide, and a mixture of two or more thereof, and the titanium source is selected from the group consisting of tetrabutylorthotitanate, tetraisopropylorthotitanate, tetra-ethylorthotitanate, titanium dioxide, titanium tetrachloride, titanium tert-butoxide, and a mixture of two or more thereof.

8. The process of claim 1 , wherein in the aqueous synthesis mixture in (ii.1), a molar ratio of Ti, calculated as TiO 2 and comprised in the titanium source, relative to Si, calculated as SiO 2 and comprised in the zeolitic material having a molar ratio B 2 O 3 :SiO 2 of at most 0.02:1, is in a range of from 0.005:1 to 0.1:1, a molar ratio of H 2 O relative to Si, calculated as SiO 2 and comprised in the zeolitic material having a molar ratio B 2 O 3 :SiO 2 of at most 0.02:1, is in a range of from 8:1 to 20:1, and a molar ratio of the MWW template compound relative to Si, calculated as SiO 2 and comprised in the zeolitic material provided in (i), is in a range of from 0.5:1 to 1.7:1.

9. The process of claim 1 , wherein in (ii.2), the hydrothermal synthesizing is carried out at a temperature in a range of from 80 to 250° C., and for a period in a range of from 10 to 100 h.

10. The process of claim 1 , wherein neither during (ii.2), nor after (ii.2) and before (iii), the titanium-comprising zeolitic material having an MWW framework structure is separated from the mother liquor.

11. The process of claim 1 , wherein the mother liquor subjected to (iii) comprising the titanium-comprising zeolitic material having an MWW framework structure has a solids content in a range of from 5 to 25 weight-% based on a total weight of the mother liquor comprising the titanium-comprising zeolitic material.

12. The process of claim 1 , wherein during spray-drying in (iii), a drying gas inlet temperature is in a range of from 200 to 700° C., and a drying gas outlet temperature is in a range of from 70 to 190° C.

13. The process of claim 1 , wherein the zeolitic material having an MWW framework structure obtained from (iii) has a Si content in a range of from 30 to 40 weight-%, calculated as elemental Si, a total organic carbon content (TOC) in a range of from 0 to 14 weight-%, and a Ti content of from 2.1 to 2.8 weight-%, calculated as elemental titanium, in each case based on a total weight of the zeolitic material, and wherein in (iii), the zeolitic material having an MWW framework structure is obtained in a form of particles having a Dv10 value in a range of from 1 to 10 micrometer, a Dv50 value in a range of from 5 to 50 micrometer, and a Dv90 value in a range of from 12 to 200 micrometer.

14. The process of claim 1 , further comprising
(iv) treating the titanium-comprising zeolitic material having an MWW framework structure obtained from (iii) with an aqueous solution having a pH of at most 5.

15. The process of claim 14 , wherein after (iii) and before (iv), the spray-dried titanium-comprising zeolitic material having an MWW framework structure obtained from (iii) is not subjected to calcination.

16. The process of claim 14 , wherein in (iv), the aqueous solution has a pH in a range of from 0 to 5.

17. The process of claim 14 , wherein in (iv), the titanium-comprising zeolitic material having an MWW framework structure is treated with the aqueous solution at a temperature in a range of from 50 to 175° C.

18. The process of claim 14 , further comprising
(v) separating the titanium-comprising zeolitic material having an MWW framework structure obtained from (iv) from the aqueous solution to obtain a separated titanium-comprising zeolitic material having an MWW framework.

19. The process of claim 18 , wherein (v) comprises drying the separated titanium-comprising zeolitic material having an MWW framework structure.

20. The process of claim 18 , further comprising
(vi) preparing a suspension and subjecting the suspension to spray-drying.

21. The process of claim 20 , further comprising
(vii) calcining the titanium-comprising zeolitic material havin

Assignees

• Basf Se

Inventors

• Parvulescu Andrei-Nicolae
• Mueller Ulrich
• Luetzel Hans-Juergen
• Uhl Georg
• Bayer Robert
• Vogelsang Regina
• Teles Joaquim Henrique
• Riedel Dominic
• Urbanczyk Daniel
• Wegerle Ulrike

Classifications

• B01J29/89

  Silicates, aluminosilicates or borosilicates of titanium, zirconium or hafnium {(B01J29/005 takes precedence)} · CPC title

• C01B39/085

  Group IVB- metallosilicates · CPC title

• B01J37/0045 Primary

  Drying a slurry, e.g. spray drying · CPC title

• B01J29/7038

  MWW-type, e.g. MCM-22, ERB-1, ITQ-1, PSH-3 or SSZ-25 · CPC title

• C01B39/06

  Preparation of isomorphous zeolites characterised by measures to replace the aluminium or silicon atoms in the lattice framework by atoms of other elements {, i.e. by direct or secondary synthesis} · CPC title