Catalyst Compositions and Processes for Making and Using Same
OwnerXiaoying Baoinventor
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Abstract
Catalyst compositions and processes for making and using same. The catalyst composition can include up to 0.025 wt % of Pt and up to 10 wt % of a promoter that can include Sn, Cu, Au, Ag, Ga, a combination thereof, or a mixture thereof disposed on a support. The support can include at least 0.5 wt % of a Group 2 element. All weight percent values are based on the weight of the support.
Claims24
A catalyst composition comprising up to 0.025 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, the support comprising at least 0.5 wt % of a Group 2 element, wherein all weight percent values are based on the weight of the support.
A process for making a catalyst composition, comprising:
- (I) preparing a slurry or a gel comprising a compound containing a Group 2 element and a liquid medium;
- (II) spray drying the slurry or the gel to produce spray dried particles comprising the Group 2 element;
- and
- (III) calcining the spray dried particles under an oxidative atmosphere to produce calcined support particles comprising the Group 2 element,
- wherein, at least one of (i), (ii), and (iii) is met:
- (i) Pt is present in the slurry or the gel in the form of a Pt-containing compound and the catalyst composition comprises catalyst particles comprising the calcined support particles having Pt disposed thereon,
- (ii) Pt is deposited on the spray dried particles by contacting the spray dried particles with a Pt-containing compound to produce Pt-containing spray dried particles and the catalyst composition comprises catalyst particles comprising the calcined support particles having Pt disposed thereon, and
- (iii) Pt is deposited on the calcined support particles by contacting the calcined support particles with a Pt-containing compound to produce Pt-containing calcined support particles and the process further comprises (IV) calcining the Pt-containing calcined support particles to produce re-calcined support particles having Pt disposed thereon, wherein the catalyst composition comprises the re-calcined support particles,
- and wherein, at least one of (iv), (v), and (vi) is met:
- (iv) a compound comprising a promoter element is present in the slurry or the gel and the catalyst composition comprises catalyst particles comprising the calcined support particles having the promoter element disposed thereon,
- (v) a compound comprising a promoter element is deposited on the spray dried particles to produce promoter-containing spray dried particles and the catalyst composition comprises catalyst particles comprising the calcined support particles having the promoter element disposed thereon, and
- (vi) a compound comprising a promoter element is deposited on the calcined support particles to produce promoter-containing calcined support particles and the process further comprises (V) calcining the promoter-containing calcined support particles to produce re-calcined support particles having the promoter element disposed thereon, wherein the catalyst composition comprises the re-calcined support particles,
- wherein:
- the promoter element comprises Sn, Cu, Au, Ag, Ga, a combination thereof, or a mixture thereof,
- the catalyst particles comprise the Pt in an amount of up to 0.025 wt % and the promoter element in an amount of up to 10 wt % based on the weight of the calcined support particles or the re-calcined support particles, and
- the catalyst particles comprise at least 0.5 wt % of the Group 2 element based on the weight of the calcined support particles or the re-calcined support particles.
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 hydrocarbon-containing feed and catalyst composition are contacted at a temperature in a range of from 300° C. to 900° C., for a time period of ≤3 hours, under a hydrocarbon partial pressure of at least 20 kPa-absolute, wherein the hydrocarbon partial pressure is the total partial pressure of any C2-C16 alkanes and any C8-C16 alkyl aromatics in the hydrocarbon-containing feed,
- the support comprises at least 0.5 wt % of a Group 2 element based on the weight of the support,
- the catalyst composition comprises up to 0.025 wt % of the 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, and
- the one or more upgraded hydrocarbons comprise at least one of a dehydrogenated hydrocarbon, a dehydroaromatized hydrocarbon, and a dehydrocyclized hydrocarbon.
Dependencies are inferred from the claim text.