Catalyst for ethane ODH
AssigneeNOVA Chemicals (International) S.A.
InventorsVasily Simanzhenkov, Xiaoliang Gao, David Jeffrey Sullivan, Leonid Modestovich Kustov, Aleksey Victorovich Kucherov, Elena Dmitrievna Finashina
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Abstract
A catalyst for oxidative dehydrogenation (ODH) of ethane with an empirical formula Mo—V—Te—Nb—Pd—O produced using a process comprising impregnation of the Pd component on the surface of the catalyst following a calcination step using a Pd compound free of halogens. The resulting catalyst can be used in both diluted and undiluted ODH processes and shows higher than expected activity without any loss of selectivity.
Claims19
A process for preparing an oxidative dehydrogenation catalyst comprising a mixed metal oxide having the empirical formula
- MoaVbTecNbdPdeOf
- wherein
- a, b, c, d, e and f are the relative atomic amounts of the elements Mo, V, Te, Nb, Pd, and O, respectively;
- and
- a is 1, b is from 0.01 to 1.0, c is from 0.01 to 1.0, d is from 0.01 to 0.1.0, e is from 0.0001 to less than 0.10, and f is dependent on the oxidation state of the other elements;
- the process comprising:
- admixing compounds of elements Mo, V, Te, and Nb, in a solvent comprising water to produce a first mixture;
- heating the first mixture in a first pressurized vessel at a temperature of from 100° C. to 200° C.;
- recovering a first insoluble material from the first pressurized vessel;
- subjecting the first recovered insoluble material to a calcining at a temperature of from 500° C. to 700° C. under an inert atmosphere to produce a calcined product;
- contacting the calcined product with an aqueous solution comprising a Pd compound to form second mixture, wherein the aqueous solution comprising the Pd compound is prepared from a Pd compound chosen from [Pd(NH3)4](NO3)2, Pd(HCO3)2, Pd(CH3COO)2 an analogous Pd containing salt, or a combination thereof;
- subjecting the second mixture to drying to provide a dried product;
- and
- recovering a second insoluble material from the dried product to provide the catalyst, and wherein the process excludes calcination after the impregnation of Pd.
Dependencies are inferred from the claim text.