Porous support-zeolite membrane composite and process for producing porous support-zeolite membrane composite
US-2017036175-A1 · Feb 9, 2017 · US
US11278846B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11278846-B2 |
| Application number | US-201716470230-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 9, 2017 |
| Priority date | Dec 16, 2016 |
| Publication date | Mar 22, 2022 |
| Grant date | Mar 22, 2022 |
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Provided is a method for preparing a defect-free DDR molecular sieve membrane. Sigma-1 molecular sieve is used as an inducing seed crystal to prepare and obtain a continuous and compact DDR molecular sieve membrane on the surface of a porous ceramic support. An ozone atmosphere or an external field assisted technology is used to remove a template in the pores of the molecular sieve membrane at a low temperature. The invention avoids the formation of intercrystal defects and cracks, an activated DDR molecular sieve membrane has a good selectivity for separating CO2, and the membrane preparation time is significantly reduced.
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What is claimed is: 1. A method for preparing a defect-free DDR zeolite membrane, comprising the following steps: Step 1 preparing a support loaded with seed crystals: adding Sigma-1 seed crystals into water to prepare a seed crystal suspension, and applying the seed crystal suspension on the surface of the porous support to obtain seed crystals; Step 2 synthesizing a DDR zeolite membrane: mixing and aging amantadine (ADA), silica source, ethylenediamine (EN) and water as a synthesis liquid; and adding the support loaded with seed crystal into the synthesis liquid for hydrothermal synthesis to generate a DDR zeolite membrane; Step 3 activating DDR zeolite membrane: treating the synthesized DDR zeolite membrane in an ozone atmosphere or by an external field assisted technology to remove the template ADA, thus obtaining the defect-free DDR zeolite membrane, wherein the aging parameters in the step 2 are as follows: aging at 20-120° C. for 1-10 h; the molar ratio of ADA, silica source, EN and water is: ADA/SiO 2 =0.01-0.2, EN/ADA=8-32, H 2 O/ADA=20-50; and the parameters of hydrothermal synthesis step are: synthesizing at 130-170° C. for 12 h-4 d. 2. The method for preparing a defect-free DDR zeolite membrane according to claim 1 , wherein the mass concentration of the Sigma-1 seed crystal in water is 0.2-2%; and the time for applying the seed crystal suspension is 5-50 s in the step 1. 3. The method for preparing a defect-free DDR zeolite membrane according to claim 1 , wherein the Sigma-1 zeolite used in the step 1 can be directly obtained by hydrothermal synthesis or treated by a high-energy ball milling method. 4. The method for preparing a defect-free DDR zeolite membrane according to claim 1 , wherein the porous support used in the step 1 is a flat plate, tubular or hollow fiber support. 5. The method for preparing a defect-free DDR zeolite membrane according to claim 1 , wherein the method for applying the seed crystal suspension may be selected from one or more of the following methods: spin coating, wiping coating, dip coating or vacuum pumping in the step 1. 6. The method for preparing a defect-free DDR zeolite membrane according to claim 1 , wherein the as-synthesized DDR zeolite membrane is treated in an ozone atmosphere or by an external field assisted technology for 10-100 h at 20-300° C., with the heating rate being 0.5-2° C./min in the step 3. 7. The method for preparing a defect-free DDR zeolite membrane according to claim 1 , wherein the external field assisted technology is selected from one or more of the following methods: ultraviolet irradiation, microwave digestion or Fenton reaction in the step 3. 8. The method for preparing a defect-free DDR zeolite membrane according to claim 7 , wherein the ultraviolet irradiation intensity is 50-600 mW/cm 2 ; the digestion solution used in the microwave digestion is a mixed solution of nitric acid and hydrogen peroxide, the power of the microwave digestion instrument is 500-2000 W, and the digestion temperature is 90-250° C.; the Fenton reagent in the Fenton reaction is a mixed solution of ferrous sulfate solution and hydrogen peroxide; wherein FeSO 4 .7H 2 O is added into the reaction solution, and the Fe 2+ concentration is controlled to be 4.0-15.0 mmol/L and the H 2 O 2 mass concentration is controlled to be 1.0-10.0%.
Heating · CPC title
Inorganic support material · CPC title
Zeolites · CPC title
Integrated processes (Diffusion and at least one other process, e.g. adsorption, absorption) · CPC title
Crystalline silica-polymorphs, e.g. silicalites {dealuminated aluminosilicate zeolites} · CPC title
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