Catalyst – solid sorbent – or support therefor: product or process – Catalyst or precursor therefor – Metal – metal oxide or metal hydroxide
Reexamination Certificate
1999-02-22
2002-08-20
Griffin, Steven P. (Department: 1754)
Catalyst, solid sorbent, or support therefor: product or process
Catalyst or precursor therefor
Metal, metal oxide or metal hydroxide
C502S325000, C502S326000, C502S327000, C502S328000, C502S330000, C502S332000, C502S337000, C502S338000, C423S594120
Reexamination Certificate
active
06436871
ABSTRACT:
BACKGROUND OF THE INVENTION
1. Field of the Invention
This invention relates to methods and materials for the dehydrogenation of alkanes, particularly the conversion of ethane to ethylene, and more particularly, to mixed oxide catalysts for oxidative dehydrogenation of ethane.
2. Background of the Invention
Ethylene can be produced by thermal cracking of hydrocarbons, and by nonoxidative dehydrogenation or oxidative dehydrogenation of ethane (ODHE). The latter process is attractive for many reasons. For example, compared to thermal cracking, high ethane conversion can be achieved at relatively low temperatures (about 400° C. or below). Unlike thermal cracking, catalytic ODHE is exothermic, requiring no additional heat to sustain reaction. Furthermore, in contrast to catalytic dehydrogenation, catalyst deactivation by coke formation should be minimal in ODHE because of the presence of oxygen in the reactor feed. Other alkanes can similarly be oxidatively dehydrogenated.
In the late seventies, Thorsteinson and coworkers first disclosed useful low temperature ODHE catalysts comprised of mixed oxides containing molybdenum, vanadium, and a third transition metal. E. M Thorsteinson et al., “The Oxidative Dehydrogenation of Ethane over Catalyst Containing Mixed oxide of Molybdenum and Vanadium,” 52
J. Catalysis
116-32 (1978). Later studies examined families of alumina-supported vanadium-containing oxide catalysts, MV and MVSb, where M is Ni, Co, Bi, and Sn. R. Juarez Lopez et al., “Oxidative Dehydrogenation of Ethane on Supported Vanadium-Containing Oxides,” 124
Applied Catalysis A: General
281-96 (1995). More recently, Schuurman and coworkers describe unsupported iron, cobalt and nickel oxide catalysts that are active in ODHE. Y. Schuurman et al., “Low Temperature Oxidative Dehydrogenation of Ethane over Catalysts Based on Group VIII Metals,” 163
Applied Catalysis A: General
227-35 (1997). Although the mixed oxide catalysts reported by Thorsteinson, Schuurman and others might be useful discoveries, they represent a small fraction of potentially active inorganic oxide mixtures.
Industrial interest has stimulated investigations into new catalysts and methods for improved performance (e.g., conversion and selectivity) for the oxidative dehydrogenation of alkanes. There is a need for new dehydrogenation catalysts and methods.
SUMMARY OF THE INVENTION
This invention discloses catalysts and methods for the oxidative dehydrogenation of alkanes that have from 2 to 4 carbon atoms and particularly ethane to ethylene. These catalysts primarily include nickel oxide and catalyze oxidative dehydrogenation with conversions of greater than 5% and with selectivity of greater than 70%. An object of the present invention is to provide a process whereby a C
2
-C
4
alkane can be oxidatively dehydrogenated to one or more olefins with relatively high levels of conversion and selectivity. A further object of this invention is to provide a catalyst that selectively catalyzes the reaction of a C
2
-C
4
alkane with oxygen to produce one or more corresponding C
2
-C
4
olefins with relatively high levels of conversion and selectivity, meaning preferably without the concurrent production of significant amounts of by-products, such as carbon monoxide or carbon dioxide.
In general, the catalysts of this invention have as a required component nickel oxide and it is an object of this invention to provide a catalyst for the oxidative dehydrogenation of an alkane into one or more olefins having nickel oxide (NiO). The nickel oxide is combined with other metal oxides, dopants, carriers, binders and/or fillers into a catalyst that is contacted with a gas mixture. The gas mixture comprises at least the alkane and oxygen, but may also include diluents (such as argon, nitrogen, etc.) or other components (such as water or carbon dioxide). Optionally, the gas mixture that contacts the catalyst may also include one or more of the olefin products for an oxidative dehydrogenation process that converts a gas mixture having one ratio of alkane to alkene to a gas mixture having a different ratio of alkane to alkene. The catalysts of this invention include a material or composition of matter having the empirical formula:
Ni
x
A
j
B
k
C
l
O
i
I
wherein
Ni is nickel and x is in the range of about 0.1-0.96;
A is selected from the group consisting of Nb, Ta, Co and combinations thereof and j is in the range of from about 0-0.8;
B is an element selected from the group consisting of alkali metals, alkaline earths, or lanthanides and combinations thereof, including Li, Na, K, Rb, Cs, Mg, Ca, Sr, Ba, Mn, La, Ce, Pr, Nd, Sm and combinations thereof and k is in the range of from 0-0.5;
C is an element selected from the group consisting of Sn, Al, Fe, Si, B, Sb, Tl, In, Ge, Cr, Pb and combinations thereof and 1 is in the range of from 0-0.5;
i is a number that satisfies the valence requirements of the other elements present; and
the sum of j, k and l is at least 0.04.
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Griffin Steven P.
Nguyen Cam N.
Pennie & Edmonds LLP
Symyx Technologies Inc.
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