Methods to produce molecular sieves with LTA topology and compositions derived therefrom

Patent metadata

Field	Value
Publication number	US-9821297-B2
Application number	US-201615063867-A
Country	US
Kind code	B2
Filing date	Mar 8, 2016
Priority date	Mar 10, 2015
Publication date	Nov 21, 2017
Grant date	Nov 21, 2017

Abstract

The present disclosure is directed to processing for preparing crystalline pure-silica and heteroatom-substituted LTA frameworks in fluoride media using a simple organic structure-directing agent (OSDA), having a structure of Formula (I):

where substituents R 1 to R 9 are defined herein. Aluminosilicate LTA is an active catalyst for the methanol to olefins reaction with higher product selectivities to butenes as well as C5 and C6 products than the commercialized catalysts. Titanosilicate LTA is an active catalyst for the epoxidation of allyl alcohol using aqueous H 2 O 2 .

First claim

What is claimed:

1. A process for comprising hydrothermally treating an aqueous composition comprising:
(a) a source of a silicon oxide;
(b) an optional source of an aluminum oxide;
(c) an optional source of a germanium oxide;
(d) an optional source of a titanium oxide;
(e) an optional source of one or more of a boron oxide, gallium oxide, hafnium oxide, iron oxide, tin oxide, indium oxide, vanadium oxide, zinc oxide, zirconium oxide, or combination or mixture thereof;
(f) a mineralizing agent; and
(g) an organic structure directing agent (OSDA) comprising a substituted benzyl-3H-imidazol-1-ium cation of Formula (I):

and optionally a tetramethylammonium salt, under conditions effective to crystallize a crystalline microporous silicate solid of LTA topology;
wherein
R 1 , R 2 , and R 7 are independently C 1-6 alkyl;
R 3 , R 4 , R 5 , R 6 , R 8 , and R 9 are independently H or C 1-3 alkyl; and

the substituted benzyl-3H-imidazol-1-ium cation has an associated bromide, chloride, fluoride, iodide, nitrate, or hydroxide anion.

2. The process of claim 1 , wherein the OSDA comprises a 2,3-dialkyl-1-(4-alkyl-benzyl)-3H-imidazol-1-ium cation of Formula (IA):

wherein R 1 , R 2 , and R 7 are independently C 1-3 alkyl.

3. The process of claim 1 , wherein the OSDA comprises a 2,3-dimethyl-1-(4-methyl-benzyl)-3H-imidazol-1-ium cation of Formula (IB):

(2,3-dimethyl-1-(4-methyl-benzyl)-3H-imidazol-1-ium).

4. The process of claim 1 , wherein the aqueous composition comprises:
(b) the source of the aluminum oxide;
(c) the source of the germanium oxide;
(d) the source of the titanium oxide; or
(e) a combination of two or more of (b)-(d).

5. The process of claim 1 , wherein the hydrothermal treatment provides a crystalline microporous pure-silicate, aluminosilicate, germanosilicate, or titanosilicate solid of LTA topology.

6. The process of claim 1 , wherein:
(a) the source of the silicon oxide comprises a silicon alkoxide, a silicate, a silica hydrogel, silicic acid, fumed silica, colloidal silica, a tetra-alkyl orthosilicate, a silica hydroxide, a silicon alkoxide, or combination thereof;
(b) the source of the aluminum oxide, when present, comprises an alkoxide, hydroxide, or oxide of aluminum, a sodium aluminate, or combination thereof;
(c) the source of the germanium oxide, when present, comprises a alkali metal orthogermanate, containing discrete GeO 4 4− ions, GeO(OH) 3 − , GeO2(OH) 2 2− , [(Ge(OH) 4 ) 8 (OH) 3 ] 3− or neutral solutions of germanium dioxide containing Ge(OH) 4 , or an alkoxide or carboxylate derivative thereof; and
(d) the source of the titanium oxide, when present, comprises a titanium alkoxide, oxide, or hydroxy oxide.

7. The process of claim 1 , wherein the mineralizing agent comprises an aqueous alkali metal or alkaline earth metal hydroxide.

8. The process of claim 1 , wherein the mineralizing agent comprises hydrofluoric acid (HF).

9. The process of claim 1 , wherein the composition has:
(a) a molar ratio of the OSDA:Si is in a range of from 0.1 to 1;
(b) a molar ratio of Al:Si in a range of from 0 to 0.1, when the source of the aluminum oxide is present;
(c) a molar ratio of Ge:Si in a range of from 0 to 1, when the source of the germanium oxide is present;
(d) a molar ratio of Ti:Si in a range of from 0 to 0.1, when the source of the titanium oxide is present;
(e) a molar ratio of water:Si in a range of from about 2 to about 20; and
(f) a molar ratio of fluoride:Si in a range of from about 0.1 to about 0.75, when the mineralizing agent is HF.

10. The process of claim 9 , wherein the aqueous composition further comprises:
(b) the source of the aluminum oxide;
(c) the source of the germanium oxide;
(d) the source of the titanium oxide; or
(e) a combination of two or more of (b)-(d).

11. The process of claim 1 , wherein the conditions effective to crystallize a crystalline microporous solid of LTA topology include treatment of the respective hydrothermally treated aqueous composition at a temperature in a range of from 100° C. to 200° C. for a time in a range of from 3 to 40 days.

12. The process of claim 1 , further comprising isolating the crystalline microporous silicate solid of LTA topology.

13. The process of claim 12 , further comprising:
(a) heating the isolated crystalline microporous solid at a temperature in a range of from about 250° C. to about 450° C.;
(b) contacting the isolated crystalline microporous solid with ozone or other oxidizing agent at a temperature in a range of 100° C. to 200° C.; or
(c) heating the isolated crystalline microporous solid at a temperature in a range of from about 200° C. to about 600° C. in the presence of an alkali, alkaline earth, transition metal, rare earth metal, ammonium or alkylammonium salt;
for a time sufficient to form a dehydrated or an OSDA-depleted product.

14. The process of claim 13 , further comprising:
(a) treating the dehydrated or OSDA-depleted product with an aqueous alkali, alkaline earth, transition metal, rare earth metal, ammonium or alkylammonium salt; and/or
(b) treating the dehydrated or OSDA-depleted product with at least one type of transition metal or transition metal oxide.

15. A crystalline microporous silicate solid of LTA topology, prepared by the process of claimed 1 , containing within its pores an OSDA comprising a substituted benzyl-3H-imidazol-1-ium cation of Formula (I):

wherein
R 1 , R 2 , and R 7 are independently C 1-6 alkyl;
R 3 , R 4 , R 5 , R 6 , R 8 , and R 9 are independently H or C 1-3 alkyl.

16. The crystalline microporous silicate solid of LTA topology of claimed 15 , wherein the solid is:
(a) a pure-silicate;
(b) an aluminosilicate;
(c) a germanosilicate; or
(d) a titanosilicate.

17. The crystalline microporous silicate solid of LTA topology of claim 15 , wherein the OSDA comprises a 2,3-dimethyl-1-(4-methyl-benzyl)-3H-imidazol-1-ium cation of Formula (IB):

18. A crystalline microporous pure-silicate, aluminosilicate, germanosilicate, or titanosilicate solid of LTA topology prepared according to the process of claim 1 .

19. The crystalline microporous pure-silicate, aluminosilicate, germanosilicate, or titanosilicate solid of claim 18 , the solid exhibiting
a powder XRD pattern having at least five characteristic peaks selected from the group consisting of 7.6° ±0.3° 2-theta; 10.6° ±0.3° 2-theta; 13.0° ±0.3° 2-theta; 15.1° ±0.3° 2-theta; 21.4° ±0.3° 2-theta; 22.7° ±0.3° 2-theta; 25.1° ±0.3° 2-theta; 27.3° ±0.3° 2-theta; 28.3° ±0.3° 2-theta; and 31.3° ±0.3° 2-theta.

20. The crystalline microporous pure-silicate, aluminosilicate, germanosilicate, or titanosilicate solid of claim 18 , the solid exhibiting a powder XRD pattern having characteristic peaks at 7.6° ±0.3° 2-theta; 10.6° ±0.3° 2-theta; 13.0° ±0.3° 2-theta; 22.7 ° ±0.3° 2-theta; and 25.1° ±0.3° 2-theta.

21. The crystalline microporous pure-silicate of claim 18 exhibiting a 29 Si Bloch

Assignees

• California Inst Of Techn

Inventors

• Boal Ben W
• Davis Mark E
• Schmidt Joel E

Classifications

• B01J29/7007

  Zeolite Beta · CPC title

• B01J29/047 Primary

  Germanosilicates; Aluminogermanosilicates (B01J29/005 takes precedence) · CPC title

• B01D2255/20707

  Titanium · CPC title

• C07D301/12

  with hydrogen peroxide or inorganic peroxides or peracids · CPC title

• B01D53/9413

  Processes characterised by a specific catalyst · CPC title