Dehydration method, dehydration apparatus, and membrane structure
US-2020101419-A1 · Apr 2, 2020 · US
US11400421B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11400421-B2 |
| Application number | US-202117444851-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 11, 2021 |
| Priority date | Mar 25, 2019 |
| Publication date | Aug 2, 2022 |
| Grant date | Aug 2, 2022 |
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In production of a zeolite membrane complex, a starting material solution containing at least a structure-directing agent and FAU-type zeolite particles having an average particle diameter of 50 to 500 nm is prepared. Then, a support is immersed in the starting material solution to form a zeolite membrane on the support by hydrothermal synthesis, the zeolite membrane being composed of AFX-type zeolite. After that, the structure-directing agent in the zeolite membrane is removed.
Opening claim text (preview).
The invention claimed is: 1. A method of producing a zeolite membrane complex, comprising: a) preparing a starting material solution containing at least a structure-directing agent and FAU-type zeolite particles having an average particle diameter of 50 to 500 nm; b) immersing a support in said starting material solution to form a zeolite membrane on said support by hydrothermal synthesis, said zeolite membrane being composed of AFX-type zeolite; and c) removing said structure-directing agent in said zeolite membrane. 2. The method of producing a zeolite membrane complex according to claim 1 , further comprising depositing seed crystals of AFX-type zeolite on said support before said operation b). 3. The method of producing a zeolite membrane complex according to claim 1 , wherein said starting material solution in said operation a) further contains silicon source and alkali source. 4. The method of producing a zeolite membrane complex according to claim 1 , wherein said FAU-type zeolite particles are composed of Y-type zeolite or X-type zeolite. 5. The method of producing a zeolite membrane complex according to claim 1 , wherein the average particle diameter of said FAU-type zeolite particles is in a range of 100 to 400 nm. 6. The method of producing a zeolite membrane complex according to claim 1 , wherein in volume-based particle diameter distribution of said starting material solution, (D90−D10)/D50 is 3 or less. 7. The method of producing a zeolite membrane complex according to claim 1 , wherein said support is porous. 8. The method of producing a zeolite membrane complex according to claim 1 , wherein said support is an alumina sintered compact, a mullite sintered compact, or a titania sintered compact. 9. A zeolite membrane complex, comprising: a support; and a zeolite membrane provided on said support, said zeolite membrane being composed of AFX-type zeolite, wherein in a cross section of said zeolite membrane which is perpendicular to a surface thereof, maximum and minimum values of thickness of said zeolite membrane in an area with a width of 10 μm in a direction along said surface are represented as A and B, respectively, and an evaluation value obtained by ((A−B)/(A+B)) is 0.04 or more and 0.70 or less. 10. The zeolite membrane complex according to claim 9 , wherein CF 4 gas permeance of said zeolite membrane complex is 10 nmol/m 2 ·s·Pa or less.
Use of template or surface directing agents [SDA] · CPC title
Reduction of greenhouse gas [GHG] emissions, e.g. CO2 · CPC title
characterised by specific membranes · CPC title
using at least one organic template directing agent · CPC title
characterised by their properties · CPC title
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