IP Library Granted Patent US 6,964,934
Granted Patent B2
US 6,964,934 · App. 10/647,854 · Granted Nov 15, 2005

Process for the preparation of doped pentasil-type zeolite using doped seeds

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Quick Facts
Patent No.
US 6,964,934
App. No.
10/647,854
Granted
Nov 15, 2005
Kind
B2
Abstract

The present invention relates to a process for the preparation of doped pentasil-type zeolite, which process comprises the steps of: a) preparing an aqueous precursor mixture from a silicon source, an aluminium source, and doped non-zeolitic seeds; and b) thermally treating the precursor mixture to form a doped pentasil-type zeolite. The term “non-zeolitic seeds” includes seeds made from materials selected from the group consisting of (i) X-ray amorphous materials, (ii) milled crystalline materials, such as milled zeolites, that have a relative crystallinity of not more than 75%, and (iii) crystalline materials other than zeolites, such as clays (e,g, bentonite and kaolin) and (low) crystalline aluminas.

Claims (13)

1. Process for the preparation of doped pentasil-type zeolite, which process comprises the steps of:

a) preparing an aqueous precursor mixture from a silicon source, an aluminium source, and doped non-zeolitic seeds, and

b) thermally treating the precursor mixture to form a doped pentasil-type zeolite.

2. The process of claim 1 wherein the doped pentasil-type zeolite is doped ZSM-5.

3. The process according of claim 1 wherein the non-zeolitic seeds are X-ray amorphous.

4. The process according of claim 1 wherein the non-zeolitic seeds are milled crystalline materials that have a relative crystallinity of not more than 75%.

5. The process of claim 4 wherein the milled crystalline materials have a relative crystallinity of not more than 60%.

6. The process of claim 5 wherein the milled crystalline materials have a relative crystallinity of not more than 50%.

7. The process of claim 1 wherein the non-zeolitic seeds are crystalline materials other than zeolites.

8. The process of claim 1 wherein the non-zeolitic seeds are doped with a dopant selected from the group consisting of Ce, La, Zr, Mn, Fe, Ti, Cu, Ni, Zn, Mo, W, V, Sn, Pt, Pd, Ga, B, and P.

9. The process of claim 1 wherein the silicon source is selected from the group consisting of sodium (meta)silicate, stabilised silica sols, silica gels, polysilicic acid, tetra ethylortho silicate, fumed silicas, precipitated silicas, and mixtures thereof.

10. The process of claim 1 wherein the aluminium source is selected from the group consisting of Al 2 (SO 4 ) 3 , AlCl 3 , AlPO 4 , Al 2 (HPO 4 ) 3 , Al(H 2 PO 4 ) 3 , aluminium trihydrate (Al(OH) 3 ), thermally treated aluminium trihydrate, (pseudo)boehmite, aluminium chlorohydrol, aluminium nitrohydrol, and mixtures thereof.

11. The process of claim 1 wherein a shaping step is performed between steps a) and b).

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 5, 2005
From: AKZO NOBEL N.V.
To: ALBEMARLE NETHERLANDS B.V.
Reel/Frame 016735/0113 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 23, 2003
From: BRADY, MIKE; LAHEIJ, ERIK JEROEN; O'CONNOR, PAUL; STAMIRES, DENNIS
To: AKZO NOBEL N.V.
Reel/Frame 014832/0331 →