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US4430096A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the production of gas mixtures containing hydrogen and carbon monoxide via the endothermic partial oxidation of organic compounds

Assignee: Hoechst AG
•
Filing: 1981-06-12
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Granted: 1984-02-07
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Expires: 2001-06-12
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Abstract

Abstract An improved process for the production of a gas mixture containing hydrogen and carbon monoxide by endothermal partial oxidization of an organic compound with steam and/or carbon dioxide is disclosed wherein at least a portion of the heat required for the partial oxidation is obtained by direct heat exchange with products obtained from the gasification of a carbonaceous ash-forming fuel with oxygen in the presence of steam.

Inventors

  • 👤 Friedrich Schnur
  • 👤 Boy Cornils
  • 👤 Josef Hibbel
  • 👤 Bern-Hard Lieder

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 04:59
CPC Classifications
C; C10; C10J; C10J3/00; C01; C01B; C01B3/00; C01B3/02; C01B3/32; C10J3/46; C10J3/48; C10J3/482; C10J3/72; C10J3/78; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0953; C10J2300/0969; C10J2300/0973; C10J2300/0976; C10J2300/18; C10J2300/1846; C10J2300/1861; C10J2300/1884; C10J2300/1892; Y; Y10; Y10S; Y10S48/00; Y10S48/02

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 180 words
A process for the production of gas mixtures containing hydrogen and carbon monoxide which comprises: A. gasifying an ash-forming solid carbonaceous fuel with oxygen or an oxygen containing gas mixture in the presence of steam in a gasifier; and B. removing liquid ash from said gasifier by entraining it in the gaseous mixture formed in said gasifier and feeding the gasified products of step A including liquid ash contained therein to a vessel into which a partially oxidizable organic compound is fed together with steam and/or carbon dioxide and therein contacting the gaseous effluent and liquid ash with steam and/or carbon dioxide introduced with said organic compound while maintaining said vessel at a temperature of 900° to 1600° C. at a pressure up to 200 bar; said contacting resulting in the cracking of the organic compound and causing the liquid ash to deposit in the solid state and recovering said ash in the solid state, and wherein said vessel contains a water bath located below the location where said contacting occurs to recover the solidified ash from the gaseous effluent.
Claim 2
Dependent Claim 180 words
A process for the production of gas mixtures containing hydrogen and carbon monoxide which comprises: A. gasifying an ash-forming solid carbonaceous fuel with oxygen or an oxygen containing gas mixture in the presence of steam in a gasifier; and B. removing liquid ash from said gasifier by entraining it in the gaseous mixture formed in said gasifier and feeding the gasified products of step A including liquid ash contained therein to a vessel into which a partially oxidizable organic compound is fed together with steam and/or carbon dioxide and therein contacting the gaseous effluent and liquid ash with steam and/or carbon dioxide introduced with said organic compound while maintaining said vessel at a temperature of 900° to 1600° C. at a pressure up to 200 bar; said contacting resulting in the cracking of the organic compound and causing the liquid ash to deposit in the solid state and recovering said ash in the solid state, and wherein said vessel contains a water bath located below the location where said contacting occurs to recover the solidified ash from the gaseous effluent.
Claim 3
Dependent Claim 15 words
A process according to claim 1 wherein the carbonaceous ash-forming fuel is finely divided coal.
Claim 4
Dependent Claim 27 words
A process according to claim 1 wherein said gasification is effected at a temperature of 1100° to 1500° C. at a pressure of 5 to 10 bar.
Claim 5
Dependent Claim 28 words
A process according to claim 1, wherein the compound to be endothermally oxidized is preheated together with steam and/or carbon dioxide before being introduced into the separating zone.
Claim 6
Dependent Claim 27 words
A process according to claim 1 wherein the organic compound to be endothermally partially oxidized is a saturated or unsaturated hydrocarbon of 1 to 3 carbon atoms.
Claim 7
Dependent Claim 22 words
A process according to claim 1 wherein the organic compound is obtained by the Fischer-Tropsch synthesis, the Oxo synthesis or is methanol.
Claim 8
Dependent Claim 14 words
A process according to claim 1, wherein said ash-forming fuel is finely divided coal.
Claim 9
Dependent Claim 58 words
A process according to claim 1, wherein said organic compound is selected from the group consisting of methane, ethane, ethylene, propane, propylene, butane, butylene, methanol, ethanol, propanol, formaldehyde, acetaldehyde, propionaldehyde, butyraldehyde, acetone, methyl ethyl ketone, diethyl ketone, dipropyl ketones, dimethyl ether, methyl ethyl ether, diethyl ether, propyl formate, butyl formate, formic acid, acetic acid, propionic acid and phenols.
Claim 10
Dependent Claim 51 words
A process according to claim 8, wherein said organic compound is selected from the group consisting of methanol, ethanol, propanol, formaldehyde, acetaldehyde, propionaldehyde, butyraldehyde, acetone, methyl ethyl ketone, diethyl ketone, dipropyl ketones, dimethyl ether, methyl ethyl ether, diethyl ether, propyl formate, butyl formate, formic acid, acetic acid, propionic acid and phenols.
Claim 11
Dependent Claim 19 words
A process according to claim 1, wherein said organic compound is fed together with carbon dioxide into said vessel.
Claim 12
Dependent Claim 60 words
A process according to claim 10, wherein said partially oxidizable organic compound is selected from the group consisting of methane, ethane, ethylene, propane, propylene, butane, butylene, methanol, ethanol, propanol, formaldehyde, acetaldehyde, propionaldehyde, butyraldehyde, acetone, methyl ethyl ketone, diethyl ketone, dipropyl ketones, dimethyl ether, methyl ethyl ether, diethyl ether, propyl formate, butyl formate, formic acid, acetic acid, propionic acid and phenols.
Claim 13
Dependent Claim 51 words
A process according to claim 10, wherein said organic compound is selected from the group consisting of methanol, ethanol, propanol, formaldehyde, acetaldehyde, propionaldehyde, butyraldehyde, acetone, methyl ethyl ketone, diethyl ketone, dipropyl ketones, dimethyl ether, methyl ethyl ether, diethyl ether, propyl formate, butyl formate, formic acid, acetic acid, propionic acid and phenols.

References Cited (Backward Citations)

US2767233A Cited
US3000711A Cited
US2987387A Cited
US3010813A Cited
US4054424A Cited
US4056483A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-02-06 1987-08-08 1988-02-07 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-02-06 1991-08-08 1992-02-07 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-02-06 1995-08-08 1996-02-07 $7700.00 Window Closed / Lapsed

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