IP Library Granted Patent US 9,895,660
Granted Patent B2
US 9,895,660 · App. 15/125,502 · Granted Feb 20, 2018

Method for producing metal exchanged microporous materials by solid-state ion exchange

Inventors: Ton V. W. Janssens (Bagsværd, DK); Peter N. R. Vennestrøm (Copenhagen S, DK)
Assignee: Haldor Topsoe A/S
B01D53/9418B01J29/061B01J29/14B01J29/46B01J29/763B01J29/85
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Quick Facts
Patent No.
US 9,895,660
App. No.
15/125,502
Granted
Feb 20, 2018
Kind
B2
Abstract

A method is disclosed for the preparation of a metal exchanged microporous materials, e.g. metal exchanged silicoaluminophosphates or metal exchanged zeolites, or mixtures of metal exchanged microporous materials, comprising the steps of providing a dry mixture of a) one or more microporous materials that exhibit ion exchange capacity and b) one or more metal compounds; heating the mixture in a gaseous atmosphere containing ammonia and one or more oxides of nitrogen to a temperature and for a time sufficient to initiate and perform a solid state ion exchange of ions of the metal compound and ions of the microporous material; and obtaining the metal-exchanged microporous material.

Claims (23)

1. Method for the preparation of a metal exchanged crystalline microporous material or mixtures of metal exchanged crystalline microporous materials comprising the steps of providing a dry mixture containing a) one or more crystalline microporous materials that exhibit ion exchange capacity and b) one or more metal compounds; heating the mixture in a gaseous atmosphere containing ammonia and one or more oxides of nitrogen to a temperature and for a time sufficient to initiate and perform a solid state ion exchange of ions of the metal compound and ions of the crystalline microporous material; and obtaining the crystalline metal-exchanged microporous material.

2. Method according to claim 1 , wherein the crystalline microporous material is selected from the group consisting of zeolite or zeotype materials.

3. Method according to claim 2 , where the zeolite or zeotype materials have the framework code of AEI, AFX, CHA, KFI, LTA, IMF, ITH, MEL, MFI, SZR, TUN, *BEA, BEC, FAU, FER, MOR, LEV.

4. Method according to claim 2 , wherein the zeolite or zeotype materials are selected from the group consisting of ZSM-5, zeolite Y, beta zeolite, SSZ-13, SSZ-39, SSZ-62, Chabazite, and SAPO-34, SAPO-44, Ferrierite, TNU-9.

5. Method according to claim 1 , wherein the crystalline microporous material or mixtures of crystalline microporous materials are in the H or NH 4 form.

6. Method according to claim 1 , wherein the crystalline microporous material or mixtures of crystalline microporous material contains an organic structure directing agent.

7. Method according to claim 1 , wherein the metal compound is selected from the group of metal oxides, metal nitrates and phosphates, sulfates, oxalates, acetates or a combination thereof.

8. Method according to claim 1 , wherein the metals in the metal compounds are selected from the group of Fe, Co, Cu.

9. Method according to claim 1 , wherein the metal compounds comprise one or more oxides of Cu.

10. Method according to claim 1 , wherein the oxide of nitrogen is selected from nitrogen monoxide, and nitrogen dioxide and mixtures thereof.

11. Method according to claim 1 , wherein the content of ammonia in the atmosphere is between 1 and 5000 vol. ppm.

12. Method according to claim 1 , wherein the content of the one or more nitrogen oxides in the gaseous atmosphere is between 1 and 5000 vol. ppm.

13. Method according to claim 1 , wherein the molar ratio of ammonia to nitrogen oxides is larger than 0.01, preferably between 0.2 and 1.

14. Method according to claim 1 , wherein the oxygen content in the atmosphere is 1% or lower.

15. Method according to claim 1 , wherein the gaseous atmosphere contains 5% water or less.

16. A method according to claim 1 , wherein the mixture is heated in the gaseous atmosphere containing ammonia and one or more oxides of nitrogen to a temperature lower than 300° C.

17. A method according to claim 1 , wherein the mixture is heated in the gaseous atmosphere containing ammonia and one or more oxides of nitrogen to a temperature in a range from 100° C. and to below 300° C.

18. A method according to claim 1 , wherein the mixture is heated in the gaseous atmosphere containing ammonia and one or more oxides of nitrogen to a temperature in a range between 150° C. and 250° C.

19. A method for the removal of nitrogen oxides from exhaust gas by selective catalytic reduction with a reductant, comprising:

preparing a catalyst comprising a metal exchanged crystalline microporous material or mixtures of metal exchanged crystalline microporous materials by: providing a dry mixture containing (a) one or more crystalline microporous materials that exhibit ion exchange capacity and (b) one or more metal compounds; heating the mixture in a gaseous atmosphere containing ammonia and one or more oxides of nitrogen to a temperature and for a time sufficient to initiate and perform a solid state ion exchange of ions of the metal compound and ions of the crystalline microporous material; and obtaining the catalyst comprising crystalline metal-exchanged microporous material; and

containing the exhaust gas with the catalyst comprising metal exchanged crystalline microporous material or mixtures of metal exchanged crystalline microporous materials.

20. A method according to claim 19 , wherein the reductant is ammonia or a precursor thereof.

21. A method according to claim 19 , wherein the reductant is hydrocarbons.

Assignments (2)
CHANGE OF NAME Recorded Oct 3, 2023
From: HALDOR TOPSØE A/S
To: TOPSOE A/S
Reel/Frame 065108/0028 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 25, 2017
From: JANSSENS, TON V.W.; VENNESTRØM, PETER N.R.
To: HALDOR TOPSOE A/S
Reel/Frame 043947/0530 →
Priority Claims (2)
DK 2014 00200 · Apr 7, 2014 · national
DK 2014 00476 · Aug 26, 2014 · national
Continuity (1)
Related Publication 20170274322A1 · Sep 28, 2017