Method of preparing expoxidation catalysts
US-2015375200-A1 · Dec 31, 2015 · US
US10434503B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10434503-B2 |
| Application number | US-201415030754-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 22, 2014 |
| Priority date | Oct 23, 2013 |
| Publication date | Oct 8, 2019 |
| Grant date | Oct 8, 2019 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The present invention relates to A process for the production of a molding, comprising (I) providing a zeolitic material; (II) mixing the zeolitic material provided in step (I) with one or more binders; (III) kneading of the mixture obtained in step (II); (IV) molding of the kneaded mixture obtained in step (III) to obtain one or more moldings; (V) drying of the one or more moldings obtained in step (IV); and (VI) calcining of the dried molding obtained in step (V); wherein the zeolitic material provided in step (I) displays a water adsorption ranging from 1 to 15 wt.-% when exposed to a relative humidity of 85%, as well as to a molding obtainable or obtained according to the inventive process in addition to a molding per se and to their respective use.
Opening claim text (preview).
The invention claimed is: 1. A process for the production of a molding, comprising: (I) providing a zeolitic material comprising hydrothermally preparing a TS-1 zeolite using a template consisting of greater than 88% to less 95% N-(2-propen-1-yl)-tri-n-propylammonium hydroxide and greater than 5% to less than 95% N-(1-propen-1-yl)-tri-n-propylammonium hydroxide; (II) mixing the zeolitic material provided in (I) with one or more binders; (III) kneading of the mixture obtained in (II); (IV) molding of the kneaded mixture obtained in (III) to obtain one or more moldings; (V) drying of the one or more moldings obtained in (IV); and (VI) calcining of the dried molding obtained in (V); wherein the zeolitic material provided in (I) displays a water adsorption ranging from 4 to 9 wt.-% when exposed to a relative humidity of 85%, wherein the water adsorption being measured under isothermal conditions at 25° C. until reaching equilibrium conditions when increasing the relative humidity from 5 to 85%. 2. The process of claim 1 , wherein the one or more binders are selected from the group consisting of inorganic binders. 3. The process of claim 1 , wherein the mixture obtained in (II) displays a weight ratio of the one or more binders to the zeolitic material (binder:zeolitic material) ranging from 0.1 to 0.6. 4. The process of claim 1 , wherein (II) further comprises mixing the zeolitic material and the one or more binders with a solvent system, wherein the solvent system comprises one or more solvents. 5. The process of claim 4 , wherein the mixture obtained in (II) displays a weight ratio of the solvent system to the zeolitic material (solvent system:zeolitic material) ranging from 0.7 to 1.7. 6. The process of claim 1 , wherein (II) further comprises mixing the zeolitic material and the one or more binders with one or more pore forming agents. 7. The process of claim 6 , wherein the mixture obtained in (II) displays a weight ratio of the one or more pore forming agents to the zeolitic material (pore forming agent:zeolitic material) ranging from 0.1 to 0.7. 8. The process of claim 6 , wherein the mixture obtained in (II) displays a weight ratio of the solvent system to the one or more binders and pore forming agents to the zeolitic material (solvent system:binder and pore forming agent:zeolitic material) ranging from (0.7-1.7):(0.4-1):1. 9. The process of claim 1 , wherein the calcining of the dried molding obtained in (V) is performed at a temperature ranging from 350 to 850° C. 10. The process of claim 1 , further comprising: (VII) subjecting the calcined molding obtained in (VI) to a hydrothermal treatment. 11. The process of claim 10 , wherein the hydrothermal treatment is performed with a water-containing solvent system and/or with an aqueous solution. 12. The process of claim 10 , wherein the hydrothermal treatment is performed for a duration ranging from 1 to 48 hours. 13. A molding, obtained by a process according to claim 1 . 14. A molding, wherein said molding contains a zeolitic material displaying a water adsorption ranging from 4 to 9 wt.-% when exposed to a relative humidity of 85%, wherein the zeolitic material comprises a hydrothermally prepared TS-1 zeolite prepared using a template consisting of greater than 88% to less 95 (N,N-(2-propen-1-yl)-tri-n-propylammonium hydroxide and greater than 5% to less than 95% N-(1-propen-1-yl)-tri-n-propylammonium hydroxide. 15. The molding of claim 14 , wherein the zeolitic material has an MFI-type framework structure comprising YO 2 and optionally comprising X 2 O 3 , wherein Y is a tetravalent element, and X is a trivalent element, said material having an X-ray diffraction pattern comprising at least the following reflections: Diffraction angle 2θ/° Intensity (%) [Cu K(alpha 1)] 55-100 7.66-8.20 40-75 8.58-9.05 92-100 22.81-23.34 49-58 23.64-24.18 16-24 29.64-30.21 14-25 44.80-45.25 16-24 45.26-45.67 wherein 100% relates to the intensity of the maximum peak in the X-ray powder diffraction pattern. 16. The molding of claim 15 , wherein the 29 Si MAS NMR of the zeolitic material comprises: a first peak (P″1) in the range of from −110.4 to −114.0 ppm; and a second peak (P″2) in the range of from −100.2 to −104.2 ppm. 17. The molding of claim 16 , wherein the deconvoluted 29 Si MAS NMR spectrum comprises one additional peak comprised in the range of from −113.2 to −115.2 ppm. 18. The molding of claim 15 , wherein at least a portion of the Y atoms and/or of the X atoms in the MFI-type framework structure is isomorphously substituted by one or more elements. 19. The molding of claim 15 , wherein a molar ratio of YO 2 to the one or more element ranges from 5 to 100. 20. The molding of claim 15 , wherein the MFI-type framework structure of the zeolitic material does not contain X 2 O 3 . 21. The molding of claim 15 , wherein Y is selected from the group consisting of Si, Sn, Ti, Zr Ge, and mixtures of two or more thereof. 22. The molding of claim 14 , wherein the zeolitic material comprises one or more cation and/or cationic elements as ionic non-framework elements. 23. The molding of claim 14 , wherein the molding further comprises one or more binders. 24. The molding of claim 14 , wherein a BET surface area of the zeolitic material contained in the molding determined according to DIN 66131 ranges from 50 to 700 m 2 /g. 25. The molding of claim 14 , wherein a specific surface area of the molding determined according to DIN 66131 ranges from 50 to 700 m 2 /g. 26. The molding of claim 14 , wherein a pore volume of the molding determined according to DIN 66133 ranges from 0.1 to 2.5 ml/g. 27. The molding of claim 14 , having a mechanical strength of from 1 to 15 N. 28. A process, comprising catalyzing a reaction with the molding of claim 14 wherein the reaction is selected from the group consisting of a reaction involving C—C bond formation, a reaction involving C—C bond conversion, an isomerization reaction, an ammoxidation reaction, a hydrocracking reaction, an alkylation reaction, an acylation reaction, a r
Silicates, aluminosilicates or borosilicates of titanium, zirconium or hafnium {(B01J29/005 takes precedence)} · CPC title
Moulding, shaping or extruding · CPC title
Physical conditioning without chemical treatment, e.g. drying, granulating, coating, irradiation · CPC title
being less than 0.5 ml/g · CPC title
Group IVB- metallosilicates · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.