IP Library Granted Patent US 7,361,328
Granted Patent B2
US 7,361,328 · App. 10/540,717 · Granted Apr 22, 2008

Method of preparing ZSM-5 using variable temperature without organic template

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Quick Facts
Patent No.
US 7,361,328
App. No.
10/540,717
Granted
Apr 22, 2008
Kind
B2
Abstract

Disclosed is a method of preparing ZSM-5 having substantially 100% crystallinity by using variable temperatures in the absence of an organic template, characterized in that a reaction mixture having a molar composition of M 2 O/SiO 2 (M: alkali metal ion) of 0.07-0.14, H 2 O/SiO 2 of 15-42 and SiO 2 /Al 2 O 3 of 20-100 is nucleated at relatively high temperatures (180-210° C.) and then crystallized at relatively low temperatures (130-170° C.), thus easily controlling a crystal size and a particle size distribution of the ZSM-5.

Claims (33)

1. A method of preparing ZSM-5, comprising the following steps of:

mixing a silica source, an alkali metal oxide source, an alumina source and water, to prepare a reaction mixture having a molar composition of M 2 O/SiO 2 (M: alkali metal ion) of 0.07-0.14, H 2 O/SiO 2 of 15-42 and SiO 2 /Al 2 O 3 of 20-100;

maintaining the reaction mixture at 180-210° C. for a reaction time controlled in a range of 2-20 hours according to an intended crystal size and a particle size distribution of the ZSM-5, to obtain a nucleated reaction mixture; and

maintaining the nucleated reaction mixture at 130-170° C. for 10-200 hours to form crystals of the ZSM-5.

2. The method as defined in claim 1 , wherein the alkali metal oxide source is alkali metal hydroxide.

3. The method as defined in claim 1 , wherein the alkali metal is sodium.

4. The method as defined in claim 1 , wherein a molar ratio of the M 2 O/SiO 2 is in the range of 0.09-0.14 when the molar ratio of the SiO 2 /Al 2 O 3 is 29 or higher.

5. The method as defined in claim 1 , wherein the molar ratio of the M 2 O/SiO 2 is in the range of 0.07-0.1 when the molar ratio of the SiO 2 /Al 2 O 3 is less than 29.

6. The method as defined in claim 1 , wherein the alumina source is sodium aluminate or aluminum hydroxide.

7. The method as defined in claim 1 , wherein the silica source is selected from the group consisting of colloidal silica, sodium silicate, white carbon and boehmite.

8. The method as defined in claim 1 , wherein the ZSM-5 has an average crystal size of 1-6 μm.

9. The method as defined in claim 8 , wherein the ZSM-5 has an average crystal size of 2-3 μm.

10. The method as defined in claim 4 , wherein the ZSM-5 has a hexagonal crystal morphology.

11. The method as defined in claim 5 , wherein the ZSM-5 has a spiral crystal morphology.

12. The method as defined in claim 5 , wherein the nucleating step is performed for 10-20 hours when the molar ratio of the SiO 2 /Al 2 O 3 is not more than 22.

13. The method as defined in claim 12 , wherein the crystallizing step is performed for 96-200 hours.

14. The method as defined in claim 1 , wherein the crystallizing step is performed until crystallinity reaches substantially 100%.

15. A method of preparing ZSM-5, comprising the following steps of:

admixing a silica source, an alkali metal oxide source and water, to prepare a first aqueous solution;

separately admixing an alumina source, an alkali metal oxide source and water, to prepare a second aqueous solution;

mixing the first aqueous solution with the second aqueous solution while being optionally added with water, to prepare a reaction mixture having a molar composition of M 2 O/SiO 2 of 0.07-0.14, H 2 O/SiO 2 of 15-42 and SiO 2 /Al 2 O 3 of 20-100;

maintaining the reaction mixture at 180-210° C. for a reaction time controlled in the range of 2-20 hours according to an intended crystal size and a particle size distribution of the ZSM-5, to obtain a nucleated reaction mixture; and

maintaining the nucleated reaction mixture at 130-170° C. for 10-200 hours to form crystals of the ZSM-5.

16. The method as defined in claim 15 , wherein the silica source in the first aqueous solution amounts to 21.5-26.7 wt %, and the alumina source in the second aqueous solution amounts to 0.9-4.4 wt %.

17. The method as defined in claim 15 , wherein the alkali metal oxide source is alkali metal hydroxide.

18. A method of preparing ZSM-5, comprising the following steps of:

admixing a silica source, an alkali metal oxide source and water, to prepare a first aqueous solution;

separately admixing an alumina source and water, to prepare a second aqueous solution;

mixing the first aqueous solution with the second aqueous solution while being optionally added with water, to prepare a reaction mixture having a molar composition of M 2 O/SiO 2 of 0.07-0.14, H 2 O/SiO 2 of 15-42 and SiO 2 /Al 2 O 3 of 20-100;

maintaining the reaction mixture at 180-210° C. for a reaction time controlled in the range of 2-20 hours according to an intended crystal size and a particle size distribution of the ZSM-5, to obtain a nucleated reaction mixture; and

maintaining the nucleated reaction mixture at 130-170° C. for 10-200 hours to form crystals of the ZSM-5.

19. The method as defined in claim 18 , wherein the silica source in the first aqueous solution amounts to 21.5-26.7 wt %, and the alumina source in the second aqueous solution amounts to 0.9-4.4 wt %.

20. The method as defined in claim 18 , wherein the alkali metal oxide source is alkali metal hydroxide.

Assignments (4)
CORRECTIVE ASSIGNMENT TO CORRECT THE INCORRECT PATENT NUMBER 7448700 AND REPLACE IT WITH 7488700 PREVIOUSLY RECORDED ON REEL 026619 FRAME 0330. ASSIGNOR(S) HEREBY CONFIRMS THE CHANGE OF NAME. Recorded Apr 11, 2016
From: SK ENERGY CO., LTD.
To: SK INNOVATION CO., LTD.
Reel/Frame 038406/0201 →
CHANGE OF NAME Recorded Jul 14, 2011
From: SK ENERGY CO., LTD.
To: SK INNOVATION CO., LTD.
Reel/Frame 026619/0330 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 14, 2007
From: SK CORPORATION
To: SK ENERGY CO., LTD
Reel/Frame 020249/0017 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 24, 2005
From: KIM, WHA-JUNG; KIM, SHIN-DONG
To: SK CORPORATION
Reel/Frame 017390/0510 →