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US4207169A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the steam dealkylation of aromatic hydrocarbons

Assignee: IFP Energies nouvelles
•
Filing: 1979-01-08
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Granted: 1980-06-10
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Expires: 1999-01-08
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Abstract

Abstract Catalytic process for steam dealkylation of a charge containing at least one alkyl aromatic hydrocarbon, such as a charge issued from effluents of units for catalytic reforming or for producing aromatic hydrocarbons, wherein the catalyst contains an alumina carrier, from 0.1 to 1% of rhodium, from 0.05 to 1% of TiO2 and optionally from 0.1 to 1% of ruthenium, palladium, iridium, platinum or osmium and/or from 0.01 to 5% of lithium, sodium, potassium, rubidium or cesium.

Inventors

  • 👤 Philippe Courty
  • 👤 Germain Martino
  • 👤 Jean-Francois Le Page

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 21:54
CPC Classifications
C; C10; C10G; C10G59/00; C10G59/02; B; B01; B01J; B01J23/00; B01J23/38; B01J23/40; B01J23/46; B01J23/54; B01J23/56; B01J23/70; B01J23/89; B01J23/8933; B01J23/8946; B01J37/00; B01J37/02; B01J37/0201; B01J37/0207; C07; C07C; C07C4/00; C07C4/08; C07C4/12; C07C4/14; C07C4/20; C07C2521/00; C07C2521/02; C07C2521/04; C07C2521/06; C07C2523/00; C07C2523/02; C07C2523/04; C07C2523/08; C07C2523/12; C07C2523/14; C07C2523/16; C07C2523/20; C07C2523/22; C07C2523/24; C07C2523/26; C07C2523/28; C07C2523/30; C07C2523/32; C07C2523/34; C07C2523/36; C07C2523/38; C07C2523/40; C07C2523/42; C07C2523/44; C07C2523/46; C07C2523/70; C07C2523/74; C07C2523/745; C07C2523/75; C07C2523/755; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52

Claims Analysis

Total Claims: 15
Claim 1
Independent Claim 50 words
A process for steam dealkylation of a charge containing at least one alkyl aromatic hydrocarbon, in the presence of a catalyst containing an alumina carrier and, expressed by weight with respect to the catalyst, from 0.1 to 1% of rhodium and 0.05 to 1% of titanium oxide TiO 2 .
Claim 2
Dependent Claim 50 words
A process for steam dealkylation of a charge containing at least one alkyl aromatic hydrocarbon, in the presence of a catalyst containing an alumina carrier and, expressed by weight with respect to the catalyst, from 0.1 to 1% of rhodium and 0.05 to 1% of titanium oxide TiO 2 .
Claim 3
Dependent Claim 32 words
A process according to claim 1 wherein the catalyst contains, expressed by weight with respect to the catalyst, from 0.2 to 0.8% of rhodium and from 0.06 to 0.5% of titanium oxide.
Claim 4
Dependent Claim 37 words
A process according to claim 2, wherein the catalyst further contains, expressed by weight with respect to the catalyst, from 0.1 to 1% of at least one noble metal selected from ruthenium, palladium, iridium, platinum and osmium.
Claim 5
Dependent Claim 37 words
A process according to claim 2, wherein the catalyst further contains, expressed by weight, with respect to the catalyst, from 0.01 to 5% of at least one alkali metal selected from lithium, sodium, potassium, rubidium and cesium.
Claim 6
Dependent Claim 37 words
A process according to claim 3, wherein the catalyst further contains, expressed by weight with respect to the catalyst, from 0.01 to 5% of at least one alkali metal selected from lithium, sodium, potassium, rubidium and cesium.
Claim 7
Dependent Claim 54 words
A process according to claim 3, wherein the catalyst further contains, expressed by weight with respect to the catalyst, from 0.01 to 6% of at least one additional metal or compound of an additional metal selected from indium, zirconium, thorium, germanium, tin, vanadium, niobium, tantalum, chromium, molybdenum, tungsten, manganese, rhenium, iron, cobalt and nickel.
Claim 8
Dependent Claim 41 words
A process according to claim 6, wherein the catalyst contains a noble metal of the platinum family selected from ruthenium, palladium and platinum and in which the additional metal or metal compound is selected from rhenium, germanium, vanadium, tantalum and niobium.
Claim 9
Dependent Claim 53 words
A process according to claim 4, wherein the catalyst further contains, expressed by weight with respect to the catalyst, from 0.01 to 6% of at least one additional metal or compound of additional metal selected from indium, zirconium, thorium, germanium, tin, vanadium, niobium, tantalum, chromium, molybdenum tungsten, manganese, rhenium, iron, cobalt and nickel.
Claim 10
Dependent Claim 61 words
A process according to claim 8, wherein the catalyst contains an alumina carrier, from 0.25 to 0.65% of rhodium, 0.07 to 0.3% of titanium oxide, an alkali metal selected from sodium, potassium and rubidium, and at least one additional metal or compound of additional metal selected from indium, tungsten, tin, manganese, chromium, molybdenum, iron, niobium, cobalt, vanadium, nickel, germanium and iron.
Claim 11
Dependent Claim 32 words
A process according to claim 9, wherein the additional metal or the compound of additional metal of the catalyst is selected from cobalt, nickel, indium, tin, chromium, molybdenum, tungsten, manganese and iron.
Claim 12
Dependent Claim 74 words
A process according to claim 5, wherein the catalyst contains an alumina carrier and, by weight, from 0.25 to 0.65% of rhodium, 0.07 to 0.3% of titanium oxide, 0.25 to 0.65% of a noble metal selected from ruthenium, palladium and platinum, an alkali metal and 0.01 to 6% of at least one additional metal or compound of additional metal selected from indium, tungsten, tin, manganese, chromium, iron, niobium, cobalt, vanadium, nickel, germanium and rhenium.
Claim 13
Dependent Claim 18 words
A process according to claim 11, wherein the catalyst contains rhodium, titanium oxide, palladium, iron, nickel and potassium.
Claim 14
Dependent Claim 14 words
A process according to claim 1, used for the dealkylation of toluene to benzene.
Claim 15
Dependent Claim 24 words
A process according to claim 1, used for dealkylating alkylaromatic hydrocarbons issued from effluents of units for catalytic reforming or for producing aromatic hydrocarbons.

References Cited (Backward Citations)

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US3197523A Cited
US3436433A Cited
US3595932A Cited
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JPS5139588A Cited
FR2317962A1 Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-06-10 1983-12-10 1984-06-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-06-10 1987-12-10 1988-06-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-06-10 1991-12-10 1992-06-10 $7700.00 Window Closed / Lapsed

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