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US4201661A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing aromatics of high purity from oil cuts

Assignee: IFP Energies nouvelles
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Filing: 1974-03-26
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Granted: 1980-05-06
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Expires: 1994-03-26
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Abstract

Abstract Aromatic hydrocarbons of high purity are produced from saturated or unsaturated gasolines and hydrogen in the presence of a new catalyst containing alumina, platinum, at least one metal selected from the group consisting of iridium, rhodium and palladium and at least one metal selected from the group consisting of copper, silver and gold.

Inventors

  • 👤 Bernard Juguin
  • 👤 Jean-Francois Le Page
  • 👤 Jean Miquel

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-24 21:59
CPC Classifications
C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/085; C10G35/09; B; B01; B01J; B01J23/00; B01J23/38; B01J23/48; B01J23/70; B01J23/89; B01J23/8926; B01J37/00; B01J37/22; C07; C07C; C07C5/00; C07C5/32; C07C5/373; C07C5/393; C07C5/41; C07C5/415; C07C5/417; C10G2400/00; C10G2400/02

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 189 words
A process for producing aromatic hydrocarbons from saturated or unsaturated gasolines, in the presence of hydrogen and a catalyst, in at least one reaction zone, each reaction zone being divided into successive steps (α) and (β) wherein step (α) is conducted at 400°-600° C. under a pressure of 1 to 60 kg/cm 2 , with a substantially neutral γ-alumina catalyst having a specific surface less than 100 m 2 /g, and step (β) is conducted at 500°-600° C. under a pressure of 1 to 60 kg/cm 2 , with an acidic catalyst, of cubic γ-alumina or chlorinated or fluorinated alumina each step being conducted at an hourly feed rate by volume of the liquid charge of about 0.1-10 times the volume of the catalyst, in the presence of a catalyst containing (a) alumina, (b) 0.01-5% by weight of platinum with respect to alumina, (c) 0.001-1% by weight with respect to alumina of at least one metal selected from the group consisting of rhodium and palladium, and (d) 0.0001-0.05% by weight with respect to alumina of at least one metal selected from the group consisting of copper, silver and gold.
Claim 2
Dependent Claim 189 words
A process for producing aromatic hydrocarbons from saturated or unsaturated gasolines, in the presence of hydrogen and a catalyst, in at least one reaction zone, each reaction zone being divided into successive steps (α) and (β) wherein step (α) is conducted at 400°-600° C. under a pressure of 1 to 60 kg/cm 2 , with a substantially neutral γ-alumina catalyst having a specific surface less than 100 m 2 /g, and step (β) is conducted at 500°-600° C. under a pressure of 1 to 60 kg/cm 2 , with an acidic catalyst, of cubic γ-alumina or chlorinated or fluorinated alumina each step being conducted at an hourly feed rate by volume of the liquid charge of about 0.1-10 times the volume of the catalyst, in the presence of a catalyst containing (a) alumina, (b) 0.01-5% by weight of platinum with respect to alumina, (c) 0.001-1% by weight with respect to alumina of at least one metal selected from the group consisting of rhodium and palladium, and (d) 0.0001-0.05% by weight with respect to alumina of at least one metal selected from the group consisting of copper, silver and gold.

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) 1983-05-06 1983-11-05 1984-05-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-05-06 1987-11-05 1988-05-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-05-06 1991-11-05 1992-05-06 $7700.00 Window Closed / Lapsed

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