Catalyst Ta-Nb for the production of 1,3-butadiene

US10792644B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10792644-B2
Application numberUS-201615744386-A
CountryUS
Kind codeB2
Filing dateJul 5, 2016
Priority dateJul 13, 2015
Publication dateOct 6, 2020
Grant dateOct 6, 2020

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

The invention relates to a catalyst that comprises a mesoporous oxide matrix, with said matrix comprising at least one oxide of an element X that is selected from among silicon and titanium, taken by itself or in a mixture, with said catalyst comprising at least the tantalum element and the niobium element, with the tantalum mass representing between 0.1 to 30% by weight of the mass of the mesoporous oxide matrix, the niobium mass representing between 0.02 to 6% by weight of the mass of the mesoporous oxide matrix, the content by mass of the tantalum element being greater than or equal to the content by mass of the niobium element. The invention also relates to the use of this catalyst in a method for the production of 1,3-butadiene from a feedstock that comprises at least ethanol.

First claim

Opening claim text (preview).

The invention claimed is: 1. A catalyst comprising a mesoporous oxide matrix, said matrix comprising at least one oxide of an element X that is silicon or titanium, alone or in a mixture, said catalyst comprising tantalum and niobium, having a tantalum mass of 0.1 to 30% of the mass of the mesoporous oxide matrix, a niobium mass of 0.02 to 6% of the mass of the mesoporous oxide matrix, the content by mass of the tantalum element in said catalyst being greater than or equal to the content by mass of the niobium element in said catalyst, said catalyst being prepared by consecutive introduction of the niobium element and then the tantalum element. 2. The catalyst according to claim 1 , in which said oxide matrix is mesostructured. 3. The catalyst according to claim 1 , in which said oxide matrix is a silicon oxide that has a specific surface area of 100 to 1,200 m 2 /g, a mesopore volume of between 0.2 and 1.8 ml/g and a mesopore diameter of between 4 and 50 nm. 4. The catalyst according to claim 3 , in which said oxide matrix contains an alkaline metal content that is expressed in terms of % by weight of metal in relation to the mass of the mesoporous matrix of less than 1% by weight. 5. The catalyst according to claim 1 , further comprising at least one element of groups 1, 2, 3, 4 of the periodic table, or mixtures thereof, with the mass of said element representing between 0.01 and 5% of the mass of said mesoporous oxide matrix. 6. The catalyst according to claim 5 , further comprising at least one element of groups 1 or 2 of the periodic table, or mixtures thereof, with the mass of said element representing between 0.01 and 5% of the mass of said mesoporous oxide matrix. 7. The catalyst according to claim 6 , comprising at least one element that is Cs, Ca, Ba, or mixtures thereof, with the mass of said element representing between 0.01 and 5% of the mass of said mesoporous oxide matrix. 8. The catalyst according to claim 1 , further comprising at least one element of groups 11 or 12 of the periodic table, or mixtures thereof, with the mass of said element representing between 0.5 and 10% of the mass of said mesoporous oxide matrix. 9. The catalyst according to claim 8 , comprising at least Zn, with the mass of Zn representing between 0.5 and 10% of the mass of said mesoporous oxide matrix. 10. A process for the production of 1,3-butadiene from a feedstock that comprises at least ethanol, comprising contacting said feedstock with a catalyst according to claim 1 , at a temperature of between 300 and 400° C., a pressure of between 0.15 and 0.5 MPa, and a volumetric flow rate of between 0.5 and 5 h −1 . 11. The process according to claim 10 , in which the temperature is between 320° C. and 380° C. 12. The process according to claim 10 , in which the pressure is between 0.15 and 0.3 MPa. 13. The process according to claim 10 , in which the volumetric flow rate is between 1 and 4 h −1 .

Assignees

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Classifications

  • Silica · CPC title

  • in the presence of water, e.g. steam · CPC title

  • to form a gel or a cogel · CPC title

  • of zinc, cadmium or mercury · CPC title

  • the impregnation liquid containing organic compounds · CPC title

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What does patent US10792644B2 cover?
The invention relates to a catalyst that comprises a mesoporous oxide matrix, with said matrix comprising at least one oxide of an element X that is selected from among silicon and titanium, taken by itself or in a mixture, with said catalyst comprising at least the tantalum element and the niobium element, with the tantalum mass representing between 0.1 to 30% by weight of the mass of the meso…
Who is the assignee on this patent?
Ifp Energies Now, Michelin & Cie
What technology area does this patent fall under?
Primary CPC classification B01J23/20. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Oct 06 2020 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 1 related publication on this page (citations in our corpus or others sharing the same primary CPC).