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US3871997A Expired / Lapsed US ⏱️ 0.0 years remaining

Novel hydrocarbon conversion catalyst and reforming use thereof

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1973-07-19
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Granted: 1975-03-18
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Expires: 1993-07-19
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Abstract

Abstract The instant invention relates to a novel hydrocarbon conversion catalyst and its uses in hydrocarbon conversion processes. The novel catalyst of the instant invention comprises platinum, iridium and rhodium on an inorganic support. Preferably, the catalyst comprises from 0.1 to 1.0 wt. % platinum, from 0.1 to 1.0 wt. % iridium, and from 0.05 to 0.5 wt. % rhodium present on the surface of the support in the form of highly dispersed polymetallic clusters. The catalyst of this invention is especially useful in reforming of naphtha.

Inventors

  • 👤 John H Sinfelt
  • 👤 Allan E Barnett
  • 👤 James L Carter

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 13:33
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/90; B01J23/96; B01J23/38; B01J23/40; B01J23/46; B01J23/468; B01J37/00; B01J37/22; C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/085; C10G35/09; C10G47/00; C10G47/02; C10G47/10; C10G47/12; C10G47/14; C07; C07C; C07C2521/00; C07C2521/02; C07C2521/04; C07C2521/06; C07C2521/08; C07C2521/12; C07C2523/00; C07C2523/38; C07C2523/40; C07C2523/42; C07C2523/46; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/584

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 117 words
A naphtha reforming catalyst comprising alumina in association with from 0.1 to 1.0 wt % platinum, from 0.1 to 1.0 wt % iridium, and from 0.05 to 0.5 wt % rhodium based on total catalyst, said platinum, iridium and rhodium being present as polymetallic clusters on said support, and said clusters having a surface area of at least 200 square meters per gram of metal as determined by carbon monoxide chemisorption techniques, said catalyst further comprising a halogen moiety in an amount of from 0.1 to 3 wt % based on total catalyst and containing less than about 2 atoms of sulfur per atom of metal and being substantially free of alkali and alkaline earth metal constituents.
Claim 2
Dependent Claim 117 words
A naphtha reforming catalyst comprising alumina in association with from 0.1 to 1.0 wt % platinum, from 0.1 to 1.0 wt % iridium, and from 0.05 to 0.5 wt % rhodium based on total catalyst, said platinum, iridium and rhodium being present as polymetallic clusters on said support, and said clusters having a surface area of at least 200 square meters per gram of metal as determined by carbon monoxide chemisorption techniques, said catalyst further comprising a halogen moiety in an amount of from 0.1 to 3 wt % based on total catalyst and containing less than about 2 atoms of sulfur per atom of metal and being substantially free of alkali and alkaline earth metal constituents.
Claim 3
Dependent Claim 66 words
The catalyst composition of claim 1 wherein said metals are present on said support in the form of dispersed polymetallic atom clusters, the metal atoms of said clusters being separated by distances varying from about 2.5 to 4.0 Angstroms, the average distance between the centers of said clusters present on said support being at least 10 times the average distance between the atoms in the clusters.
Claim 4
Dependent Claim 108 words
A HYDROCARBON REFORMING PROCESS WHICH COMPRISES CONTACTING A NORMALLY LIQUID HYDROCARBON MATERIAL AT REFORMING CONDITIONS AND IN THE PRESENCE OF HYDROGEN WITH A CATALYST COMPRISING FROM 0.1 TO 1.0 WT% RHODIUM BASED ON TOTAL % IRIDIUM AND FROM 0.05 TO 0.5 WT% RHODIUM BASED ON TOTAL CATALYST WEIGHT SUPPORTED ON A REFRACTORY INORGANIC OXIDE SUPPORT, SAID PLATINUM, IRIDIUM AND RHODIUM BEING PRESENT AS METALS HAVING A SURFACE AREA OF AT LEAST 200 SQUARE METERS PER GRAM AS DETERMINED BY CARBON MONOXIDE CHEMISORPTION TECHNIQUES, SAID CATALYST CONTAINING LESS THAN ABOUT 2 ATOMS OF SULFUR PER ATOM OF METAL AND BEING SUBSTANTIALLY FREE OF ALKALI AND ALKALINE EARTH METAL CONSTITUENTS.
Claim 5
Dependent Claim 108 words
A HYDROCARBON REFORMING PROCESS WHICH COMPRISES CONTACTING A NORMALLY LIQUID HYDROCARBON MATERIAL AT REFORMING CONDITIONS AND IN THE PRESENCE OF HYDROGEN WITH A CATALYST COMPRISING FROM 0.1 TO 1.0 WT% RHODIUM BASED ON TOTAL % IRIDIUM AND FROM 0.05 TO 0.5 WT% RHODIUM BASED ON TOTAL CATALYST WEIGHT SUPPORTED ON A REFRACTORY INORGANIC OXIDE SUPPORT, SAID PLATINUM, IRIDIUM AND RHODIUM BEING PRESENT AS METALS HAVING A SURFACE AREA OF AT LEAST 200 SQUARE METERS PER GRAM AS DETERMINED BY CARBON MONOXIDE CHEMISORPTION TECHNIQUES, SAID CATALYST CONTAINING LESS THAN ABOUT 2 ATOMS OF SULFUR PER ATOM OF METAL AND BEING SUBSTANTIALLY FREE OF ALKALI AND ALKALINE EARTH METAL CONSTITUENTS.
Claim 6
Dependent Claim 24 words
The process of claim 3 wherein said catalyst additionally contains from about 0.1 to 3 wt % of a halogen based on total catalyst.
Claim 7
Dependent Claim 10 words
The process of claim 4 wherein said halogen is chlorine.
Claim 8
Dependent Claim 34 words
The process of claim 5 wherein said normally liquid hydrocarbon material is contacted with said catalyst at a temperature varying from 650* to 1,000*F and at a pressure varying from 1 to 50 atmospheres.
Claim 9
Dependent Claim 10 words
The process of claim 6 wherein said support is alumina.

References Cited (Backward Citations)

US2992985A Cited
US2848377A Cited
US3109038A Cited
US3410789A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-03-17 1978-09-16 1979-03-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-03-17 1982-09-16 1983-03-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-03-17 1986-09-16 1987-03-18 $7700.00 Window Closed / Lapsed

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