Method for preparing defect-free ddr molecular sieve membrane
US-2019366274-A1 · Dec 5, 2019 · US
US2021213396A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2021213396-A1 |
| Application number | US-202117148699-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jan 14, 2021 |
| Priority date | Jan 15, 2020 |
| Publication date | Jul 15, 2021 |
| Grant date | — |
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The present invention relates to a method of controlling a defect structure in an MFI zeolite membrane and a method of separating xylene isomers using the MFI zeolite membrane produced by the method, and more particularly, to a method of controlling a defect structure in an MFI zeolite membrane that improves the performance of separating a xylene isomer by reducing the amount and size of defects formed in the MFI membrane structure when removing organic-structure-directing agents in the membrane through calcination at a low temperature using ozone.
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1 . A method of controlling a defect structure in an MFI zeolite membrane comprising calcining the MFI zeolite membrane under ozone environment at a temperature of 100 to 300° C. 2 . The method of controlling a defect structure in an MFI zeolite membrane of claim 1 , wherein ozone is fed in a total amount of 0.05 to 75 vol % at a rate of ozone feeding of 0.001 to 1.5 g/min, and calcination is conducted at a temperature increase rate of 0.1 to 20° C./min for 0.5 to 168 hours. 3 . The method of controlling a defect structure in an MFI zeolite membrane of claim 1 , wherein the MFI zeolite membrane is produced by a method comprising adding a secondary growth solution containing an organic-structure-directing agent, SiO 2 , H 2 O, Al 2 O 3 and Na 2 O at a molar ratio of 1 to 100:5 to 500:1,000 to 50,000:0 to 100:0 to 1,000 to a support, on which an MFI seed layer is formed, and conducting hydrothermal synthesis. 4 . The method of controlling a defect structure in an MFI zeolite membrane of claim 3 , wherein the organic-structure-directing agent is at least one selected from the group consisting of TPAOH (tetrapropylammonium hydroxide), TPABr (tetrapropylammonium bromide), TPAF (tetrapropylammonium fluoride), TPACl (tetrapropylammonium chloride), TPAI (tetrapropylammonium iodide), TEAOH (tetraethylammonium hydroxide), TEABr (tetraethylammonium bromide), TEAF (tetraethylammonium fluoride), TEACl (tetraethylammonium chloride) and TEAI (tetraethylammonium iodide). 5 . The method of controlling a defect structure in an MFI zeolite membrane of claim 3 , wherein the hydrothermal synthesis is performed at a temperature of 80 to 200° C. for 12 to 240 hours. 6 . The method of controlling a defect structure in an MFI zeolite membrane of claim 3 , further comprising, after the hydrothermal synthesis, drying the membrane at a temperature of 30 to 200° C. for 1 to 24 hours. 7 . The method of controlling a defect structure in an MFI zeolite membrane of claim 3 , wherein the support is at least one selected from the group consisting of alpha-alumina, polypropylene, polyethylene, polytetrafluoroethylene, polysulfone, polyimide, silica, glass, gamma-alumina, mullite, zirconia, titania, yttria, ceria, vanadia, silicon, stainless steel and carbon. 8 . A method of separating p-xylene from a mixture of C8 aromatic isomers using the MFI zeolite membrane produced by the method of claim 1 . 9 . The method separating p-xylene from a mixture of C8 aromatic isomers of claim 8 , wherein the C8 aromatic isomer is p-xylene, m-xylene, o-xylene, or ethylbenzene. 10 . The method separating p-xylene from a mixture of C8 aromatic isomers of claim 8 , wherein the separation is performed at a temperature of 50° C. or higher.
Zeolites · CPC title
Inorganic additives · CPC title
Heating · CPC title
by sintering · CPC title
Inorganic support material · CPC title
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