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US4492772A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the production of oxygenated hydrocarbons by the catalytic conversion of synthesis gas

Assignee: BP PLC
•
Filing: 1982-10-13
•
Granted: 1985-01-08
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Expires: 2002-10-13
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Abstract

Abstract An oxygenated hydrocarbon product comprising methanol and ethanol is produced by hydrogenating carbon monoxide at a temperature in the range 150 DEG to 450 DEG C. and a pressure in the range 1 to 700 bars in the presence as catalyst of a supported mixture of the metals rhodium, silver, zirconium and molybdenum and optionally also one or more of the metals iron, manganese, rhenium, tungsten, ruthenium, chromium, thorium and potassium. The preferred support is silica.

Inventors

  • 👤 William J. Ball
  • 👤 Leonard Cotton
  • 👤 David G. Stewart

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 20:30
CPC Classifications
C; C10; C10L; C10L1/00; C10L1/02; B; B01; B01J; B01J23/00; B01J23/38; B01J23/54; B01J23/66; B01J23/68; B01J23/683; B01J23/686; B01J23/688; B01J23/70; B01J23/89; B01J23/8933; B01J23/8993; B01J29/00; B01J29/04; B01J29/06; B01J29/076; C07; C07C; C07C1/00; C07C1/02; C07C1/04; C07C1/0425; C07C1/043; C07C1/0435; C07C29/00; C07C29/15; C07C29/151; C07C29/153; C07C29/156; C07C29/157; C07C29/158; C07C31/00; C07C31/02; C07C31/04; C07C31/08; C07C45/00; C07C45/49; C07C51/00; C07C51/10; C07C2521/00; C07C2521/02; C07C2521/04; C07C2521/06; C07C2521/08; C07C2521/10; C07C2521/12; C07C2521/18; C07C2523/00; C07C2523/02; C07C2523/04; C07C2523/12; C07C2523/16; C07C2523/24; C07C2523/26; C07C2523/28; C07C2523/30; C07C2523/32; C07C2523/34; C07C2523/36; C07C2523/38; C07C2523/40; C07C2523/46; C07C2523/48; C07C2523/50; C07C2523/54; C07C2523/66; C07C2523/68; C07C2523/70; C07C2523/74; C07C2523/745; C07C2529/00; C07C2529/04; C07C2529/06; C07C2529/064; C07C2529/068; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 59 words
A process for the production of an oxygenated hydrocarbon product comprising methanol and ethanol which process comprises contacting synthesis gas at a temperature in the range 150° to 450° C. and a pressure in the range 1 to 700 bars with a catalyst comprising a mixture of the metals rhodium, silver, zirconium and molybdenum incorporated on the same support.
Claim 2
Dependent Claim 59 words
A process for the production of an oxygenated hydrocarbon product comprising methanol and ethanol which process comprises contacting synthesis gas at a temperature in the range 150° to 450° C. and a pressure in the range 1 to 700 bars with a catalyst comprising a mixture of the metals rhodium, silver, zirconium and molybdenum incorporated on the same support.
Claim 3
Dependent Claim 22 words
A process according to claim 1 wherein the support is either silica, alumina, silica-alumina, magnesia, thoria, titania, chromia, zirconia or active carbon.
Claim 4
Dependent Claim 11 words
A process according to claim 1 wherein the support is silica.
Claim 5
Dependent Claim 13 words
A process according to claim 1 wherein the support is a crystalline zeolite.
Claim 6
Dependent Claim 31 words
A process according to any one of the previous claims wherein the amount of each of the metals on the support is in the range from 0.1 to 10 weight percent.
Claim 7
Dependent Claim 54 words
a process according to claim 5 wherein there is incorporated on the support a cocatalyst comprising one or more of the metals iron, manganese, rhenium, tungsten, ruthenium, chromium, thorium and potassium in an amount in the range from 0.1 to 10 weight percent based on the combined weight of the metals and the support.
Claim 8
Dependent Claim 18 words
A process according to claim 5 wherein the temperature is in the range from 200° to 400° C.
Claim 9
Dependent Claim 18 words
A process according to claim 5 wherein the pressure is in the range from 20 to 300 bars.
Claim 10
Dependent Claim 23 words
A process according to claim 5 when operated in continuous manner at a gas hourly space velocity greater than 10 3 per hour.
Claim 11
Dependent Claim 24 words
A process according to claim 9 wherein the gas hourly space velocity is in the range from 10 4 to 10 6 per hour.

References Cited (Backward Citations)

EP0030110A1 Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-01-08 1988-07-09 1989-01-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-01-08 1992-07-09 1993-01-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-01-08 1996-07-09 1997-01-08 $7700.00 Window Closed / Lapsed

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