US4201661A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for producing aromatics of high purity from oil cuts
Assignee: IFP Energies nouvelles
•
Filing: 1974-03-26
•
Granted: 1980-05-06
•
Expires: 1994-03-26
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 20:16
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)
US2752289A
Cited
US2848377A
Cited
US2911357A
Cited
US3156735A
Cited
US3585253A
Cited
US3567625A
Cited
US3617518A
Cited
US3850747A
Cited
US3729408A
Cited
US3789020A
Cited
US3769201A
Cited
US3901827A
Cited
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 |