Method for manufacturing zeolite membrane structure
US-10625215-B2 · Apr 21, 2020 · US
US12138598B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12138598-B2 |
| Application number | US-201916704091-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 5, 2019 |
| Priority date | Jun 7, 2017 |
| Publication date | Nov 12, 2024 |
| Grant date | Nov 12, 2024 |
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A dehydration method is a dehydration method for selectively separating water from a mixture that contains water, and the method includes a step of supplying the mixture to a supply side space of a separation membrane, and a step of making a pressure difference between the supply side space and a permeation side space of the separation membrane. The separation membrane includes a first zeolite membrane that faces the permeation side space and is constituted by a first zeolite and a second zeolite membrane that faces the supply side space and is adjacent to the first zeolite membrane. The second zeolite membrane is constituted by a second zeolite that has the same framework structure as framework of the first zeolite and has a lower Si/Al atom ratio than a Si/Al atom ratio of the first zeolite.
Opening claim text (preview).
The invention claimed is: 1. A dehydration apparatus comprising: a separation vessel including a separation membrane that selectively separates water from a mixture containing water, and a housing portion that is sectioned by the separation membrane into a supply side space to which the mixture is supplied and a permeation side space to which water permeated through the separation membrane flows out; and a pressure changing apparatus configured to increase the pressure in the supply side space and/or reduce the pressure in the permeation side space, wherein the separation membrane includes a first zeolite membrane that faces the permeation side space, and a second zeolite membrane that faces the supply side space and is adjacent to the first zeolite membrane, a first zeolite that constitutes the first zeolite membrane contains at least a silicon atom and an oxygen atom, and a second zeolite that constitutes the second zeolite membrane has a framework structure that is the same as a framework structure of the first zeolite, the second zeolite has a lower Si/Al atom ratio than a Si/Al atom ratio of the first zeolite, and the second zeolite contains at least a silicon atom, an aluminum atom, an oxygen atom, and at least one type of atom selected from the group consisting of alkali metals, alkaline earth metals, and hydrogen; wherein the framework structure of the first zeolite and the second zeolite is MFI. 2. The dehydration apparatus according to claim 1 , wherein the first zeolite is a high-silica zeolite, and the second zeolite is a low-silica zeolite. 3. A dehydration method for selectively separating water from a mixture that contains water, using the dehydration apparatus according to claim 1 , the method comprising: a step of supplying the mixture to a supply side space of the separation membrane; and a step of making a pressure difference between the supply side space and a permeation side space of the separation membrane, wherein the separation membrane includes: a first zeolite membrane configured to face the permeation side space and is constituted by a first zeolite; and a second zeolite membrane configured to face the supply side space and is adjacent to the first zeolite membrane, and the second zeolite membrane is constituted by a second zeolite that has a same framework structure as framework of the first zeolite and has a lower Si/Al atom ratio than a Si/Al atom ratio of the first zeolite. 4. The dehydration method according to claim 3 , wherein the first zeolite is a high-silica zeolite, and the second zeolite is a low-silica zeolite. 5. The dehydration method according to claim 3 , wherein the framework structure of the first zeolite and the second zeolite is any one of MFI, DDR, MEL, BEA, or CHA. 6. The dehydration method according to claim 3 , wherein the framework structure of the first zeolite and the second zeolite is MFI or MEL.
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