Process for preparing a molecular sieve

Patent metadata

Field	Value
Publication number	US-10745285-B2
Application number	US-201815984595-A
Country	US
Kind code	B2
Filing date	May 21, 2018
Priority date	Feb 4, 2015
Publication date	Aug 18, 2020
Grant date	Aug 18, 2020

Abstract

A process for converting a feedstock comprising an organic compound to a conversion product by contacting said feedstock at organic compound conversion conditions with a catalyst comprising a mordenite zeolite having a mesoporous surface area of greater than 30 m2/g and an average primary crystal size as measured by TEM of less than 80 nm.

First claim

The invention claimed is:

1. A process for converting a feedstock comprising an organic compound to a conversion product which comprises the step of contacting said feedstock at organic compound conversion conditions with a catalyst comprising a mordenite zeolite having a mesopore surface area of greater than 30 m 2 /g and comprising agglomerates composed of primary crystallites, wherein the primary crystallites have an average primary crystal size as measured by TEM of less than 80 nm.

2. The process of claim 1 , wherein the primary crystallites have an average primary crystal size of less than 80 nm in each of the a, b and c crystal vectors as measured by X-ray diffraction.

3. The process of claim 1 , wherein at least 90% by number of the primary crystallites have a primary crystal size of less than 80 nm as measured by TEM.

4. The process of claim 1 , wherein said primary crystallites have an aspect ratio of less than 2, wherein the aspect ratio is defined as the longest dimension of the crystallite divided by the width of the crystallite, where the width of the crystallite is defined as the dimension of the crystallite in the middle of that longest dimension in a dimension orthogonal to that longest dimension, as measured by TEM.

5. The process of claim 1 , wherein the mordenite zeolite has a mesopore surface area of greater than 40 m 2 /g.

6. The process of claim 1 , wherein the ratio of mesopore surface area to the total surface area is greater than 0.05.

7. The process of claim 1 , wherein the mordenite zeolite is a calcined mordenite zeolite prepared by subjecting the mordenite zeolite to a calcining step, the calcined mordenite zeolite having a mesopore surface area of greater than 30 m 2 /g and comprising agglomerates composed of primary crystallites, wherein the primary crystallites have an average primary crystal size as measured by TEM of less than 80 nm.

8. The process of claim 7 , wherein the calcined mordenite zeolite has a Si:Al 2 molar ratio greater than or equal to 50.

9. The process of claim 1 , wherein the mordenite zeolite is made by a method comprising the steps of:
(a) providing a synthesis mixture comprising a silicon source, an aluminum source, an alkali metal (M) hydroxide, a source of a structure directing agent (SDA) selected from the group consisting of TEA, MTEA and mixtures thereof, optionally seed crystals and water, said synthesis mixture having a composition including the following molar ratios:
Si:Al 2 15-40
OH − :Si≤0.32
M + :Si≤0.32
SDA:Si≤0.10
H 2 O:Si<20

(b) subjecting said synthesis mixture to crystallization conditions which include heating the synthesis mixture at a temperature in the range of from 100° C. to 160° C. to form crystals of a mordenite zeolite comprising the structure directing agent (SDA) within its pores.

10. The process of claim 9 , wherein the silicon source is a precipitated silica.

11. The process of claim 9 , wherein the aluminum source is a sodium aluminate solution or an aluminum sulfate solution.

12. The process of claim 9 , wherein the SDA source is selected from the group consisting of tetraethylammonium bromide (TEABr), tetraethylammonium hydroxide (TEAOH), methyltriethylammonium chloride (MTEACl), methyltriethylammonium hydroxide (MTEAOH), and mixtures thereof.

13. The process of claim 9 , wherein the mordenite zeolite is a calcined mordenite zeolite made by a method which comprises the steps of:
(i) subjecting the mordenite zeolite of claim 9 to an ion exchange treatment to remove alkali metal cation M + , and then
(ii) calcining the mordenite zeolite at a temperature of equal to or greater than 500° C. for a period of at least 1 hour.

14. The process of claim 13 , further comprising a dealumination step which comprises:
(iii) contacting the calcined mordenite zeolite with steam at a temperature of at least 200° C. for a duration of at least one hour, and then washing with an aqueous acid solution.

Assignees

• Exxonmobil Chemical Patents Inc

Inventors

• Lai Wenyih F
• Rollman Nicholas S
• Cao Guang

Classifications

• B01J35/45

  Nanoparticles · CPC title

• B01J35/70

  characterised by their crystalline properties, e.g. semi-crystalline (catalysts comprising carbon B01J21/18; molecular sieves B01J29/00) · CPC title

• B01J35/77

  Compounds characterised by their crystallite size · CPC title

• B01J2235/30

  Scanning electron microscopy; Transmission electron microscopy · CPC title

• B01J2235/15

  X-ray diffraction · CPC title