IP Library Granted Patent US 8,376,148
Granted Patent B2
US 8,376,148 · App. 13/219,277 · Granted Feb 19, 2013

Inorganic porous support-zeolite membrane composite, production method thereof, and separation method using the composite

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Quick Facts
Patent No.
US 8,376,148
App. No.
13/219,277
Granted
Feb 19, 2013
Kind
B2
Abstract

An object of the present invention is to provide a zeolite membrane composite satisfying both the treating amount and the separation performance at a practically sufficient level, which can be applied even in the presence of an organic material and can separate/concentrate an organic material-containing gas or liquid mixture and which is economic without requiring a high energy cost and is not limited in its application range; a production method thereof; and a separation or concentration method using the same. The present invention is an inorganic porous support-zeolite membrane composite, wherein the inorganic porous support contains a ceramic sintered body and the inorganic porous support-zeolite membrane composite has, as a zeolite membrane, a CHA-type zeolite crystal layer on the inorganic porous support surface.

Claims (25)

1. An inorganic porous support-zeolite membrane composite, wherein the inorganic porous support contains a ceramic sintered body and the inorganic porous support-zeolite membrane composite has, as the zeolite membrane, a CHA-type zeolite crystal layer on the inorganic porous support surface, and in the X-ray diffraction pattern obtained by irradiating the zeolite membrane surface with an X-ray, the peak intensity near 2θ=17.9° is 0.5 times or more the peak intensity near 2θ=20.8°.

2. An inorganic porous support-zeolite membrane composite, wherein the inorganic porous support-zeolite membrane composite has a CHA-type zeolite crystal layer as the zeolite membrane and in the X-ray diffraction pattern obtained by irradiating the zeolite membrane surface with an X-ray, the peak intensity near 2θ=17.9° is 0.5 times or more the peak intensity near 2θ=20.8°.

3. An inorganic porous support-zeolite membrane composite, wherein the inorganic porous support-zeolite membrane composite has a CHA-type zeolite crystal layer as the zeolite membrane and in the X-ray diffraction pattern obtained by irradiating the zeolite membrane surface with an X-ray, the peak intensity near 2θ=9.6° is 4 times or more the peak intensity near 2θ=20.8°.

4. The inorganic porous support-zeolite membrane composite as claimed in claim 1 , wherein in the X-ray diffraction pattern obtained by irradiating the zeolite membrane surface with an X-ray, the peak intensity near 2θ=9.6° is 4 times or more the peak intensity near 2θ=20.8°.

5. The inorganic porous support-zeolite membrane composite as claimed in claim 1 , wherein the molar ratio SiO 2 /Al 2 O 3 of the zeolite crystal layer is 5 or more.

6. The inorganic porous support-zeolite membrane composite as claimed in claim 1 , wherein the inorganic porous support comprises at least one kind of a material selected from the group consisting of alumina, silica and mullite.

7. A method for producing the inorganic porous support-zeolite membrane composite claimed in any one of claims 1 to 3 , which comprises crystallizing a CHA-type zeolite on the inorganic porous support surface.

8. The method of producing the inorganic porous support-zeolite membrane composite as claimed in claim 7 , wherein after attaching a zeolite seed crystal to the inorganic porous support surface, the CHA-type zeolite is crystallized.

9. The method of producing the inorganic porous support-zeolite membrane composite as claimed in claim 8 , wherein the zeolite seed crystal is a CHA-type zeolite.

10. The method of producing the inorganic porous support-zeolite membrane composite as claimed in claim 7 , wherein in performing crystallization of the CHA-type zeolite, a reaction mixture containing an Si element source and an Al element source is used as a raw material such that the molar ratio (SiO 2 /Al 2 O 3 ) as the ratio between Si and Al in terms of respective oxides becomes from 5 to 10,000.

11. The method of producing the inorganic porous support-zeolite membrane composite as claimed in claim 10 , wherein an alkali metal ion is present in the reaction mixture.

12. The method of producing the inorganic porous support-zeolite membrane composite as claimed in claim 10 , wherein an organic template is further used as a raw material and the organic template is a cation derived from 1-adamantanamine.

13. A separation membrane comprising the inorganic porous support-zeolite membrane composite claimed in claim 1 .

14. A separation method comprising contacting an organic material-containing gas or liquid mixture with the inorganic porous support-zeolite membrane composite claimed in any one of claims 1 to 3 to allow for permeation of a highly permeable substance out of said mixture, thereby separating said highly permeable substance from said mixture.

15. The separation method as claimed in claim 14 , wherein the organic material-containing gas or liquid mixture is a mixture of an organic acid and water.

16. The separation method as claimed in claim 14 , wherein the organic material-containing gas or liquid mixture is a mixture of water and at least one kind of a material selected from organic compounds containing an alcohol, an ether, an aldehyde, a ketone or a nitrogen.

17. A concentration method comprising contacting an organic material-containing gas or liquid mixture with the inorganic porous support-zeolite membrane composite claimed in any one of claims 1 to 3 to allow for permeation of a highly permeable substance out of said mixture, thereby concentrating the highly permeable substance.

18. The concentration method as claimed in claim 17 , wherein the organic material-containing gas or liquid mixture is a mixture of water and at least one kind of a material selected from organic compounds containing an alcohol, an ether, an aldehyde, a ketone or a nitrogen.

19. The inorganic porous support-zeolite membrane composite as claimed in claim 2 , wherein in the X-ray diffraction pattern obtained by irradiating the zeolite membrane surface with an X-ray, the peak intensity near 2θ=9.6° is 4 times or more the peak intensity near 2θ=20.8°.

20. The inorganic porous support-zeolite membrane composite according to claim 2 , wherein the molar ratio SiO 2 /Al 2 O 3 of the zeolite crystal layer is 5 or more.

21. The inorganic porous support-zeolite membrane composite according to claim 3 , wherein the molar ratio SiO 2 /Al 2 O 3 of the zeolite crystal layer is 5 or more.

22. The inorganic porous support-zeolite membrane composite according to claim 2 , wherein the inorganic porous support comprises at least one kind of a material selected from the group consisting of alumina, silica and mullite.

23. The inorganic porous support-zeolite membrane composite according to claim 3 , wherein the inorganic porous support comprises at least one kind of a material selected from the group consisting of alumina, silica and mullite.

24. A separation membrane comprising the inorganic porous support-zeolite membrane composite according to claim 2 .

25. A separation membrane comprising the inorganic porous support-zeolite membrane composite according to claim 3 .

Assignments (3)
CHANGE OF NAME Recorded Sep 5, 2017
From: MITSUBISHI RAYON CO., LTD.
To: MITSUBISHI CHEMICAL CORPORATION
Reel/Frame 043750/0834 →
MERGER Recorded Sep 4, 2017
From: MITSUBISHI CHEMICAL CORPORATION
To: MITSUBISHI RAYON CO., LTD.
Reel/Frame 043750/0207 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 18, 2011
From: SUGITA, MIKI; TAKEWAKI, TAKAHIKO; OSHIMA, KAZUNORI; FUJITA, NAOKO
To: MITSUBISHI CHEMICAL CORPORATION
Reel/Frame 027080/0193 →