Agglomerated ODH catalyst
US-10661256-B2 · May 26, 2020 · US
US11654419B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11654419-B2 |
| Application number | US-202117236669-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 21, 2021 |
| Priority date | Mar 26, 2018 |
| Publication date | May 23, 2023 |
| Grant date | May 23, 2023 |
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Mixed metal oxide catalysts having an amorphous content of not less than 40 wt. % are prepared by calcining the catalyst precursor fully or partially enclosed by a porous material having a melting temperature greater than 600° C. in an inert container including heating the catalyst precursor at a rate from 0.5 to 10° C. per minute from room temperature to a temperature from 370° C. to 540° C. under a stream of pre heated gas chosen from steam and inert gas and mixtures thereof at a pressure of greater than or equal to 1 psig having a temperature from 300° C. to 540° C. and holding the catalyst precursor at that temperature for at least 2 hours and cooling the catalyst precursor to room temperature.
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What is claimed is: 1. A method to calcine a catalyst precursor of the formula Mo 1 V 0.1-1 Nb 0.1-1 Te 0.01-0.2 X 0-2 O d where X is chosen from Pd, Sb Ba, Al, W, Ga, Bi, Sn, Cu, Ti, Fe, Co, Ni, Cr, Zr, Ca, oxides thereof and mixtures thereof, and d is a number to satisfy the valence of the catalyst while maintaining an amorphous content of not less than 40 wt. % the method comprising calcining the catalyst precursor in an inert container with flow passage there through, at a rate from 0.5 to 10° C. per minute from room temperature to a holding temperature from 370° C. to 540° C. under a stream of pre heated gas chosen from steam and inert gas and mixtures thereof at a rate of flow comparable to a flow rate of not less than 150 sccm through a 2.54 cm diameter tube with a length of 152 cm, at a pressure of greater than or equal to 1 psig, said stream of pre heated gas having a temperature from 300° C. to 540° C.; holding the catalyst precursor at the holding temperature for at least 2 hours; and cooling the catalyst precursor to room temperature, said catalyst precursor being fully or partially enclosed by a porous material having a melting temperature greater than 600° C. 2. The method according to claim 1 , wherein the inert container is made from high temperature glass, quartz, ceramics, or steel. 3. The method according to claim 2 , wherein the inert container has a heat conductivity greater than 0.34 W m −1 ·K. 4. The method according to claim 1 , wherein the pressure of inert gas is greater than 1 psig. 5. The method according to claim 4 , wherein rate for heating the catalyst precursor is 0.9 to 2.0° C. per min. 6. The method according to claim 4 , wherein the catalyst precursor is held at the holding temperature from 2-24 hours. 7. The method according to claim 6 , wherein the holding temperature is from 400° C. to 525° C. 8. The method according to claim 7 , wherein the inert gas comprises nitrogen. 9. The method according to claim 8 , wherein the porous material is chosen from glass and mineral fiber. 10. The method according to claim 9 , wherein charcoal or activated carbon is present on an outer surface of the porous material in an amount up to 0.5 g per 1 g of catalyst precursor. 11. The method according to claim 10 , wherein X is one or more metals and oxides thereof are chosen from Pd, Sb, Ba, Al, Cu, Ti, Fe, Ca, Zr and mixtures thereof. 12. The method according to claim 11 , wherein the molar ratio of said one or more metals and oxides chosen from Pd, Sb, Ba, Al, Cu, Ti, Fe, Ca, Zr and mixtures thereof to Mo is from 1:0.001-0.3. 13. The method according to claim 12 , wherein the X is chosen from of one or more metals and oxides thereof are chosen from Pd, Sb, Ba, Al, Cu and mixtures thereof. 14. The method according to claim 1 , wherein in the catalyst precursor X is absent. 15. The method according to claim 14 , wherein the catalyst precursor has the formula: Mo 1.0 V 0.10-0.49 Te 0.06-0.17 Nb 0.13-0.19 O d .
Indexing scheme associated with group B01J35/00, related to the analysis techniques used to determine the catalysts form or properties · CPC title
characterised by their amorphous structures · CPC title
Scanning electron microscopy; Transmission electron microscopy · CPC title
characterised by their crystalline properties, e.g. semi-crystalline (catalysts comprising carbon B01J21/18; molecular sieves B01J29/00) · CPC title
X-ray diffraction · CPC title
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