Catalyst Compositions and Processes for Making and Using Same
OwnerYi Du, Bradley D. Wooler +1inventors
InventorsYi Du, Bradley D. Wooler, Xiaoying Bao
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Abstract
Catalyst compositions and processes for making and using same. The catalyst composition can include up to 6 wt % of Pt and up to 10 wt % of a promoter comprising Sn, Cu, Au, Ag, Ga, a combination thereof, or a mixture thereof disposed on a support, based on the weight of the support. The support can include a mixed Mg/A metal oxide. The support can have a surface area>300 m2/g.
Claims25
A catalyst composition comprising a support and, based on the weight of the support, up to 6 wt % of Pt and up to 10 wt % of a promoter comprising Sn, Cu, Au, Ag, Ga, a combination thereof, or a mixture thereof disposed on the support, wherein:
- the support comprises a mixed Mg/Al metal oxide, and
- the support has a surface area >300 m2/g.
A process for making a catalyst composition, comprising:
- (I) combining a first compound comprising Mg, a second compound comprising Al, a first base compound, water, and optionally a Pt-containing compound and/or a promoter-containing compound under agitation conditions for a time sufficient to produce a slurry or a gel comprising a plurality of precursor support particles comprising water disposed thereon and/or therein;
- (II) contacting the slurry or the gel with an organic solvent to displace at least a portion of the water from the slurry or the gel to produce a plurality of precursor support particles comprising the organic solvent disposed thereon and/or therein, wherein optionally a Pt-containing compound and/or a promoter-containing compound is contacted with (i) the slurry or the gel or (ii) with the plurality of precursor support particles comprising the organic solvent disposed thereon and/or therein;
- (III) removing at least a portion of the organic solvent from the plurality of precursor support particles to produce a plurality of dried precursor support particles, wherein optionally a Pt-containing compound and/or a promoter-containing compound is contacted with the dried precursor support particles;
- and
- (IV) heating the plurality of dried precursor support particles to a temperature of at least 350° C., to produce a plurality of calcined support particles, wherein optionally a Pt-containing compound and/or a promoter-containing compound is contacted with the plurality of calcined support particles, wherein:
- the Pt-containing compound and the promoter-containing compound are independently present in at least one of steps (I), (II), (III), and (IV),
- the catalyst composition comprises up to 6 wt % of Pt and up to 10 wt % of the promoter, based on the weight of the plurality of calcined support particles,
- the promoter comprises Sn, Cu, Au, Ag, Ga, a combination thereof, or a mixture thereof,
- the plurality of calcined support particles comprises a mixed Mg/Al metal oxide, and
- the plurality of calcined support particles has a surface area ≥300 m2/g.
A process for upgrading a hydrocarbon, comprising:
- (I) contacting a hydrocarbon-containing feed with a catalyst composition comprising Pt and a promoter disposed on a support to effect one or more of dehydrogenation, dehydroaromatization, and dehydrocyclization of at least a portion of the hydrocarbon-containing feed to produce a coked catalyst composition and an effluent comprising one or more upgraded hydrocarbons and molecular hydrogen, wherein:
- the hydrocarbon-containing feed comprises one or more of C2-C16 linear or branched alkanes, or one or more of C4-C16 cyclic alkanes, or one or more C8-C16 alkyl aromatics, or a mixture thereof,
- the catalyst composition comprises up to 6 wt % of Pt and up to 10 wt % of the promoter, based on the weight of the support,
- the promoter comprises Sn, Cu, Au, Ag, Ga, a combination thereof, or a mixture thereof,
- the support comprises a mixed Mg/Al metal oxide, and
- the support has a surface area ≥300 m2/g.
Dependencies are inferred from the claim text.