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Process for preparing a synthesis gas suitable as starting material for the oxo-synthesis

Assignee: Hoechst AG
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Filing: 1975-12-02
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Granted: 1977-09-13
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Expires: 1995-12-02
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Abstract

Abstract In an oxo process, a gas mixture of approximately equal amounts of hydrogen and carbon monoxide for re-use in the process is made by catalytically cracking the "thick oil" residue from the oxo step at elevated temperatures in presence of water vapor and carbon dioxide over a supported metal catalyst.

Inventors

  • 👤 Jurgen Falbe
  • 👤 Heinz-Dieter Hahn

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 20:02
CPC Classifications
C; C01; C01B; C01B3/00; C01B3/02; C01B3/32; C01B3/22; C01B3/34; C01B3/38

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 185 words
In an oxo process wherein an olefin is hydroformylated to an oxygen-containing product having one or more carbon atom than said olefin, and wherein after recovery of said product there remains a thick oil residue comprising aldehydes, alcohols, acetals, aldols and esters, the improved method of converting said thick oil to useful product comprising cracking said thick oil over a supported nickel catalyst containing in the range of 2 to 25 weight percent nickel in the presence of in the range of 1.5 to 2.5 moles water vapor and 1.6 to 3.0 moles carbon dioxide per g-atom in said thick oil, and at a temperature in the range of 600° C to 900° C and a pressure in the range up to 30 atmospheres, recovering from the material so cracked a synthesis gas mixture consisting essentially of carbon monoxide and hydrogen, and controlling the amount and properties of said water vapor and carbon dioxide used to yield a hydrogen/carbon monoxide ratio in said synthesis gas mixture in the approximate range of 1:1 to 2:1 and rcycling said hydrogen and carbon monoxide to said oxo process.
Claim 2
Dependent Claim 185 words
In an oxo process wherein an olefin is hydroformylated to an oxygen-containing product having one or more carbon atom than said olefin, and wherein after recovery of said product there remains a thick oil residue comprising aldehydes, alcohols, acetals, aldols and esters, the improved method of converting said thick oil to useful product comprising cracking said thick oil over a supported nickel catalyst containing in the range of 2 to 25 weight percent nickel in the presence of in the range of 1.5 to 2.5 moles water vapor and 1.6 to 3.0 moles carbon dioxide per g-atom in said thick oil, and at a temperature in the range of 600° C to 900° C and a pressure in the range up to 30 atmospheres, recovering from the material so cracked a synthesis gas mixture consisting essentially of carbon monoxide and hydrogen, and controlling the amount and properties of said water vapor and carbon dioxide used to yield a hydrogen/carbon monoxide ratio in said synthesis gas mixture in the approximate range of 1:1 to 2:1 and rcycling said hydrogen and carbon monoxide to said oxo process.
Claim 3
Dependent Claim 18 words
The process of claim 1 wherein said olefin is selected from the group consisting of propylene and ethylene.
Claim 4
Dependent Claim 23 words
The process of claim 2 wherein the recycled synthesis gas mixture, after initial start-up, is the sole synthesis gas supplied to said hydroformulation.
Claim 5
Dependent Claim 43 words
The process of claim 1 wherein said catalyst contains in the range of 5 to 20 weight percent nickel, said temperature is in the range of 700° C to 800° C and said pressure is in the range of 15 to 25 atm.

References Cited (Backward Citations)

US3451949A Cited
US3454364A Cited
US3556751A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-09-12 1981-03-14 1981-09-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-09-12 1985-03-14 1985-09-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-09-12 1989-03-14 1989-09-13 $7700.00 Window Closed / Lapsed

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