← Back to Patent Explorer
US4235801A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing ethanol from synthesis gas

Assignee: Union Carbide Corp
•
Filing: 1976-04-12
•
Granted: 1980-11-25
•
Expires: 1996-04-12
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A process for the selective preparation of ethanol by continuously contacting a synthesis gas reaction mixture containing hydrogen and carbon monoxide with a rhodium-iron catalyst.

Inventors

  • 👤 Madan M. Bhasin

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 00:54
CPC Classifications
C; C07; C07C; C07C45/00; C07C45/49; B; B01; B01J; B01J23/00; B01J23/70; B01J23/89; B01J23/8906; C07C29/00; C07C29/15; C07C29/151; C07C29/153; C07C29/156; C07C29/157; C07C29/158; C07C51/00; C07C51/10; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 166 words
In a process for the reaction of a synthesis gas containing carbon monoxide and hydrogen in the presence of a hydrogenation catalyst, the improvement whereby oxygenated hydrocarbon products of two-carbon atoms are selectively produced, which comprises continuously contacting said synthesis gas with a heterogeneous catalyst consisting essentially of a combination of rhodium and iron and at reaction conditions correlated to achieve product efficiencies based on cabon consumption in excess of 10 percent and obtain the formation of ethanol, and optionally acetic acid and/or acetaldehyde as well, in an amount which is at least about 50 weight percent of the two or more carbon atom compounds obtained by the reaction and there is obtained an increased amount of ethanol relative to that produced when the catalyst is rhodium only, which reaction conditions include a temperature within the range of about 150°-450° C., a pressure within the range of about 15-10,000 psig, and a mole ratio of hydrogen to carbon monoxide within the range of 20:1 to 1:20.
Claim 2
Dependent Claim 166 words
In a process for the reaction of a synthesis gas containing carbon monoxide and hydrogen in the presence of a hydrogenation catalyst, the improvement whereby oxygenated hydrocarbon products of two-carbon atoms are selectively produced, which comprises continuously contacting said synthesis gas with a heterogeneous catalyst consisting essentially of a combination of rhodium and iron and at reaction conditions correlated to achieve product efficiencies based on cabon consumption in excess of 10 percent and obtain the formation of ethanol, and optionally acetic acid and/or acetaldehyde as well, in an amount which is at least about 50 weight percent of the two or more carbon atom compounds obtained by the reaction and there is obtained an increased amount of ethanol relative to that produced when the catalyst is rhodium only, which reaction conditions include a temperature within the range of about 150°-450° C., a pressure within the range of about 15-10,000 psig, and a mole ratio of hydrogen to carbon monoxide within the range of 20:1 to 1:20.
Claim 3
Dependent Claim 44 words
Process of claim 1 wherein said reaction conditions include a temperature within the range of about 250°-350° C., a pressure within the range of about 300-5,000 psig, and a mole ratio of hydrogen to carbon monoxide within the range of about 5:1 to 1:5.
Claim 4
Dependent Claim 39 words
Process of claim 1 wherein said combination of rhodium and iron is present on a support in amounts within the range of about 0.1 to about 25 weight percent based on the combined weight of the metal and support.
Claim 5
Dependent Claim 21 words
Process of claim 1 wherein said support is selected from the group consisting of alpha alumina, gamma alumina, and silica gel.
Claim 6
Dependent Claim 20 words
Process of claim 1 wherein the space velocity of the synthesis gas is in excess of about 10 3 GHSV.
Claim 7
Dependent Claim 20 words
Process of claim 5 wherein said space velocity is within the range of about 10 4 to 10 6 GHSV.

References Cited (Backward Citations)

No citation records indexed.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-11-25 1984-05-26 1984-11-25 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-11-25 1988-05-26 1988-11-25 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-11-25 1992-05-26 1992-11-25 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag