Process for making molecular sieves
US-2020062604-A1 · Feb 27, 2020 · US
US10974231B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10974231-B2 |
| Application number | US-201816608997-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 30, 2018 |
| Priority date | Apr 28, 2017 |
| Publication date | Apr 13, 2021 |
| Grant date | Apr 13, 2021 |
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The present invention provides a method for preparing hierarchical zeolite and hierarchical zeolite prepared thereby. The method includes the steps of: carrying out a reaction of a mixture containing water, a silica precursor, an alumina precursor, a pH adjustment material, at least one structure-inducing material, and at least one surfactant; and carrying out drying and heat treatment. The structure-inducing material and the surfactant have different carbon atoms while the surfactant has more carbon atoms than the structure-inducing material.
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The invention claimed is: 1. A method for manufacturing a hierarchical EU-2 zeolite, comprising: reacting a mixture comprising water, a silica precursor, an alumina precursor, a pH adjusting material, at least one structural directing agent and at least one surfactant; and drying and heat-treating, wherein the structural directing agent and the surfactant have different numbers of carbon atoms, and the surfactant has a larger number of carbon atoms than the structural directing agent, and wherein the mixture comprises the structural directing agent at a molar ratio of 1/160 to 1/38 to silica. 2. The method of claim 1 , wherein a main chain of the structural directing agent has 10 carbon atoms or less and has an ammonium functional group, and a main chain of the surfactant has 11 carbon atoms or more and has an ammonium functional group. 3. The method of claim 1 , wherein the structural directing agent is at least one selected from the group consisting of tetramethylammonium bromide, tetramethylammonium chloride, tetramethylammonium hydroxide, tetraethylammonium bromide, tetraethylammonium chloride, tetraethylammonium hydroxide, tetraethylammonium tetrafluoroborate, hexamethonium chloride, hexamethonium bromide. 4. The method of claim 1 , wherein the surfactant is at least one selected from the group consisting of cetyltrimethylammonium bromide, cetyltrimethylammonium chloride and cetylpyridinium chloride. 5. The method of claim 1 , wherein the silica precursor is at least one selected from the group consisting of fumed silica, precipitated silica, colloidal silica, sodium silicate, tetramethyl orthosilicate, tetraethyl ortho silicate, borosilicate and fluorosilicate. 6. The method of claim 1 , wherein the alumina precursor is at least one selected from the group consisting of sodium aluminate, sodium aluminum sulfate and aluminum. 7. The method of claim 1 , wherein the pH adjusting material is at least one selected from the group consisting of lithium hydroxide, sodium hydroxide, potassium hydroxide, rubidium hydroxide, cesium hydroxide and ammonium hydroxide. 8. The method of claim 1 , wherein the mixture comprises the silica at a molar ratio of 0.05 to 0.13 to water. 9. The method of claim 1 , wherein the mixture comprises the surfactant at a molar ratio of 1/200 to 1/20 to the silica. 10. The method of claim 1 , wherein the mixture comprises an EU-2 seed. 11. The method of claim 1 , wherein the reaction is carried out at a temperature range of 140° C. to 190° C. for 24 hours to 72 hours. 12. The method of claim 1 , wherein the mixture is reacted after mixing for 30 minutes to 24 hours. 13. The method of claim 1 , wherein the mixture is gelled at 25° C. to 80° C. for 3 hours to 24 hours. 14. An EU-2 zeolite having an EU-2 crystal structure and comprising Micropores having a diameter of smaller than 2 nm and mesopores having a diameter of 2 nm to 50 nm hierarchically connected to each other, wherein the micropores have a volume of 0.060 cm 3 /g to 0.09 cm 3 /g. 15. The EU-2 zeolite of claim 14 , wherein the EU-2 zeolite has a surface area of the micropores of 140 m 2 /g to 240 m 2 /g and a surface area of the mesopores of 40 m 2 /g to 110 m 2 /g. 16. The EU-2 zeolite of claim 14 , wherein the EU-2 zeolite has a silica to alumina molar ratio (SAR) of 90 to 160. 17. The EU-2 zeolite of claim 14 , wherein the EU-2 zeolite has a total BET surface area of 190 m 2 /g to 310 m 2 /g. 18. The EU-2 zeolite of claim 14 , wherein the EU-2 zeolite has a second hierarchical index of 0.50 to 0.90.
X-ray diffraction · CPC title
characterised by their crystalline properties, e.g. semi-crystalline (catalysts comprising carbon B01J21/18; molecular sieves B01J29/00) · CPC title
containing crystalline alumino-silicates, e.g. molecular sieves · CPC title
Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof · CPC title
EUO-type, e.g. EU-1, TPZ-3 or ZSM-50 · CPC title
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