Thin, porous metal sheets and methods for making the same
US-9079136-B2 · Jul 14, 2015 · US
US10953372B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10953372-B2 |
| Application number | US-201916272885-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 11, 2019 |
| Priority date | May 21, 2009 |
| Publication date | Mar 23, 2021 |
| Grant date | Mar 23, 2021 |
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Zeolite membrane sheets for separation of mixtures containing water are provided, as well as methods for making the same. Thin, but robust, zeolite membrane sheets having an inter-grown zeolite crystal film directly on a thin, less than 200 micron thick, porous support sheet free of any surface pores with a size above 10 microns. The zeolite membrane film thickness is less than about 10 microns above the support surface and less than about 5 microns below the support surface. Methods of preparing the membrane are disclosed which include coating of the support sheet surface with a seed coating solution containing the parent zeolite crystals with mean particle sizes from about 0.5 to 2.0 microns at loading of 0.05-0.5 mg/cm2 and subsequent growth of the seeded sheet in a growth reactor loaded with a growth solution over a temperature range of about 45° C. to about 120° C.
Opening claim text (preview).
I claim: 1. A hydrocarbon-permeable membrane sheet for selective removal of hydrocarbon molecules from a mixture comprising: a hydrocarbon-selective membrane layer comprising inter-grown MFI-type zeolite crystals comprising SiO2/Al2O3 and disposed on a support surface of a porous metal-based support sheet, wherein the porous metal-based support sheet is less than 200 μm thick and is substantially free of surface pores greater than 10 μm in diameter, wherein substantially free is less than 1% of the surface, wherein the membrane layer has thickness above the support surface in the range of about 2 to 20 μm and has a penetration depth below the support surface in the range of about 1 μm to about 10 μm, wherein the permeable membrane sheet has a hydrocarbon permeance greater than 1×10-6 mol/m2/Pa/s and a hydrocarbon selectivity greater than 2, and wherein the membrane sheet is bendable from a substantially flat configuration to a configuration having a radius greater than ½″ (1.3 cm) without cracking. 2. The membrane sheet of claim 1 , wherein the hydrocarbon-selective membrane layer is configured to remove alcohols from alcohol-water mixtures. 3. The membrane sheet of claim 1 , wherein the porous metal-based support sheet has a porosity between 15 and 55%. 4. The membrane sheet of claim 1 , wherein the porous metal-based support sheet has a porosity between 30 and 45%. 5. The membrane sheet of claim 1 , wherein the porous metal-based support sheet comprises greater than 60% by weight of Ni, an Ni alloy, or stainless steel. 6. The membrane sheet of claim 1 , wherein the MFI-type zeolite crystals have a SiO2/Al2O3 molar ratio greater than 100.
Inorganic support material · CPC title
Nickel · CPC title
by sintering · CPC title
Heating · CPC title
Flat membranes · CPC title
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