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US4435607A Expired / Lapsed US ⏱️ 0.0 years remaining

Dehydrogenation of dehydrogenatable hydrocarbons

Assignee: Honeywell UOP LLC
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Filing: 1982-09-22
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Granted: 1984-03-06
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Expires: 2002-09-22
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Abstract

Abstract Dehydrogenatable hydrocarbons may be subjected to a dehydrogenation reaction in which the hydrocarbons are treated with a dehydrogenation catalyst such as a modified iron compound in the presence of steam in a multi-catalyst bed system. The reaction mixture containing unconverted hydrocarbon, dehydrogenated hydrocarbon, hydrogen and steam is then contacted with a selective oxidation catalyst such as a noble metal of Group VIII of the Periodic Table, a metal of Group IVA of the Periodic Table and, if so desired, a metal of Group IA or IIA of the Periodic Table composited on a highly porous inorganic support. The oxidation catalyst will selectively oxidize the hydrogen to improve the combustion thereof and supply the necessary heat required for a subsequent dehydrogenation treatment.

Inventors

  • 👤 Tamotsu Imai

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-23 19:35
CPC Classifications
C; C07; C07C; C07C15/00; C07C15/40; C07C15/42; C07C15/44; C07C15/46; C07C5/00; C07C5/32; C07C5/321; C07C5/322; C07C5/327; C07C5/333; C07C5/3332; C07C5/42; C07C5/48; Y; Y02; Y02P; Y02P20/00; Y02P20/10

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 289 words
A process for the dehydrogenation of a dehydrogenatable hydrocarbon with separate and intermediate selective oxidation of hydrogen which compises: (a) contacting said hydrocarbon with a dehydrogenation catalyst comprising an alkaline metal-promoted iron compound in a first reaction-dehydrogenation zone in the presence of steam to produce a first reaction-dehydrogenation zone effluent stream comprising a mixture of uncoverted hydrocarbons, dehydrogenated hydrocarbons, hydrogen and steam; (b) removing said first-reaction dehydrogenation zone effluent from said first reaction-dehydrogenation zone; (c) passing said removed first-reaction dehydrogenation zone effluent of step (b) to a second-reaction oxidation zone, which is separate and discrete from said-reaction dehydrogenation zone; (d) contacting said first-reaction dehydrogenation zone effluent in said second-reaction oxidation zone with an oxygen-containing gas to selectively oxidize said hydrogen within said first-reaction dehydrogenation zone effluent to the substantial exclusion of oxidation of said unconverted and dehydrogenated hydrocarbons in the presence of an oxidation catalyst consisting essentially of about 0.01 to about 5 wt% of a Group VIII noble metal, about 0.01 to about 5wt% of a Group IVA metal, and from about 0.01 to about 10% by weight of a metal of Group IA or IIA composited on a highly porous alumina support at oxidation conditions, wherein said exothermic selective oxidation of said hydrogen provides additional heat and thereby raises the temperature of said unconverted and dehydrogenated hydrocarbons; (e) withdrawing said unconverted and dehydrogenated hydrocarbons from said second-reaction oxidation zone having an increased temperature with respect to the temperature of said first-reaction dehydrogenation effluent zone; (f) passing said removed second reaction-oxidation zone product stream of step (e) to a third-reaction dehydrogenation zone, containing a dehydrogenation catalyst comprising an alkaline metal promoted iron compound at dehydrogenation conditions to produce dehydrogenated hydrocarbons; and (g) withdrawing and recovering said dehydrogenated hydrocarbons.
Claim 2
Dependent Claim 289 words
A process for the dehydrogenation of a dehydrogenatable hydrocarbon with separate and intermediate selective oxidation of hydrogen which compises: (a) contacting said hydrocarbon with a dehydrogenation catalyst comprising an alkaline metal-promoted iron compound in a first reaction-dehydrogenation zone in the presence of steam to produce a first reaction-dehydrogenation zone effluent stream comprising a mixture of uncoverted hydrocarbons, dehydrogenated hydrocarbons, hydrogen and steam; (b) removing said first-reaction dehydrogenation zone effluent from said first reaction-dehydrogenation zone; (c) passing said removed first-reaction dehydrogenation zone effluent of step (b) to a second-reaction oxidation zone, which is separate and discrete from said-reaction dehydrogenation zone; (d) contacting said first-reaction dehydrogenation zone effluent in said second-reaction oxidation zone with an oxygen-containing gas to selectively oxidize said hydrogen within said first-reaction dehydrogenation zone effluent to the substantial exclusion of oxidation of said unconverted and dehydrogenated hydrocarbons in the presence of an oxidation catalyst consisting essentially of about 0.01 to about 5 wt% of a Group VIII noble metal, about 0.01 to about 5wt% of a Group IVA metal, and from about 0.01 to about 10% by weight of a metal of Group IA or IIA composited on a highly porous alumina support at oxidation conditions, wherein said exothermic selective oxidation of said hydrogen provides additional heat and thereby raises the temperature of said unconverted and dehydrogenated hydrocarbons; (e) withdrawing said unconverted and dehydrogenated hydrocarbons from said second-reaction oxidation zone having an increased temperature with respect to the temperature of said first-reaction dehydrogenation effluent zone; (f) passing said removed second reaction-oxidation zone product stream of step (e) to a third-reaction dehydrogenation zone, containing a dehydrogenation catalyst comprising an alkaline metal promoted iron compound at dehydrogenation conditions to produce dehydrogenated hydrocarbons; and (g) withdrawing and recovering said dehydrogenated hydrocarbons.
Claim 3
Dependent Claim 32 words
The process as set forth in claim 1 in which said alkaline metal of said dehydrogenation catalyst is selected from the group consisting of Group IA and IIA of the Periodic Table.
Claim 4
Dependent Claim 36 words
The process as set forth in claim 1 in which said dehydrogenation catalyst contains an oxide or sulfide of a metal selected from the group consisting of Groups IVB, VB and VIB of the Periodic Table.
Claim 5
Dependent Claim 43 words
The process as set forth in claim 1 in which said dehydrogenation and oxidation conditions include a temperature in the range of from about 500° to about 700° C. and a pressure in the range of from about 0.1 to about 10 atmospheres.
Claim 6
Dependent Claim 15 words
The process as set forth in claim 1 in which said oxygen-containing gas is oxygen.
Claim 7
Dependent Claim 15 words
The process as set forth in claim 1 in which said oxygen-containing gas is air.
Claim 8
Dependent Claim 28 words
The process as set forth in claim 1 in which said oxidation catalyst also consists essentially of a metal of Group IA or IIA of the Periodic Table.
Claim 9
Dependent Claim 31 words
The process as set forth in claim 1 in which the noble metal of Group VIII of the Periodic Table is selected from the group consisting of platinum, palladium and rhodium.
Claim 10
Dependent Claim 30 words
The process as set forth in claim 1 in which the metal of Group IVA of the Periodic Table is selected from the group consisting of germainum, tin and lead.
Claim 11
Dependent Claim 34 words
The process as set forth in claim 1 in which the metal of Group IA or IIA of the Periodic Table is selected from the group consisting of potassium, rubidium, cesium, strontium and barium.
Claim 12
Dependent Claim 21 words
The process as set forth in claim 1 in which the dehydrogenatable hydrocarbon is ethylbenzene and said dehydrogenated hydrocarbon is styrene.

References Cited (Backward Citations)

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-03-06 1987-09-05 1988-03-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-03-06 1991-09-05 1992-03-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-03-06 1995-09-05 1996-03-06 $7700.00 Window Closed / Lapsed

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