GB659712A - Synthesis of oxygenated organic compounds - Google Patents

Synthesis of oxygenated organic compounds

Info

Publication number
GB659712A
GB659712A GB27084/49A GB2708449A GB659712A GB 659712 A GB659712 A GB 659712A GB 27084/49 A GB27084/49 A GB 27084/49A GB 2708449 A GB2708449 A GB 2708449A GB 659712 A GB659712 A GB 659712A
Authority
GB
United Kingdom
Prior art keywords
carbonyl
liquid
decobalter
butane
gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB27084/49A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Standard Oil Development Co
Original Assignee
Standard Oil Development Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Standard Oil Development Co filed Critical Standard Oil Development Co
Priority to GB27084/49A priority Critical patent/GB659712A/en
Publication of GB659712A publication Critical patent/GB659712A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C27/00Processes involving the simultaneous production of more than one class of oxygen-containing compounds
    • C07C27/20Processes involving the simultaneous production of more than one class of oxygen-containing compounds by oxo-reaction
    • C07C27/22Processes involving the simultaneous production of more than one class of oxygen-containing compounds by oxo-reaction with the use of catalysts which are specific for this process

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

In the Oxo synthesis of aldehydes and alcohols, the liquid oxygenated product is treated to decompose the dissolved metal carbonyl, and the deposited metal is recovered by contact in the treating zone with a gas rich in carbon monoxide, and a liquid organic solvent for the metol carbonyl, boiling not substantially above 210 DEG F., under conditions to yield a solution of metal carbonyl which, after adjusting its concentration, may be returned to the synthesis zone. The gas rich in CO is preferably synthesis gas. Liquid butane or pentane or similar saturated hydrocarbons may be used as solvents which are removable from the carbonyl by simple flashing. Part of the liquid olefin feed may, alternatively, be used. Other solvents are ether, methanol, acetone, and halogenated hydrocarbons. Conditions for formation and removal of cobalt carbonyl in the decobalter are suitably 200-350 DEG F., CO partial pressures of 1000-1500 p.s.i., and solvent feed rates of 0.5-5 vols./vol. decobalter space/hr. Two decobalters are preferably used alternately for metal deposition and carbonyl formation. Olefins of 6-8 carbon atoms, and CO, H2 mixture pass through a reactor which is preferably packed with crinkled wire screen or wire screen Berl saddles and fed with catalyst in the form of a solution of cobalt carbonyl in liquid butane. Reaction products are cooled, gas separated, and supplied to a decobalter, which may be at a lower pressure and about 250-400 DEG F., to which hydrogen is fed, cobalt being deposited. The effluent is treated to separate liquid products which may be hydrogenated, and gases which may be recycled to the reactor or, after CO removal, to the decobalter. When required, synthesis gas and liquid butane instead of hydrogen are fed to the decobalter, the effluent being freed of gas, at least part of the butane flashed off, and the carbonyl solution fed to the reactor. If all the butane is flashed off, the carbonyl is taken up in liquid olefin feed.
GB27084/49A 1949-10-21 1949-10-21 Synthesis of oxygenated organic compounds Expired GB659712A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB27084/49A GB659712A (en) 1949-10-21 1949-10-21 Synthesis of oxygenated organic compounds

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB27084/49A GB659712A (en) 1949-10-21 1949-10-21 Synthesis of oxygenated organic compounds

Publications (1)

Publication Number Publication Date
GB659712A true GB659712A (en) 1951-10-24

Family

ID=22066398

Family Applications (1)

Application Number Title Priority Date Filing Date
GB27084/49A Expired GB659712A (en) 1949-10-21 1949-10-21 Synthesis of oxygenated organic compounds

Country Status (1)

Country Link
GB (1) GB659712A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1138751A2 (en) * 2000-03-27 2001-10-04 Toyota Jidosha Kabushiki Kaisha Method of manufacturing oxygenated fuel

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1138751A2 (en) * 2000-03-27 2001-10-04 Toyota Jidosha Kabushiki Kaisha Method of manufacturing oxygenated fuel
EP1138751A3 (en) * 2000-03-27 2002-12-18 Toyota Jidosha Kabushiki Kaisha Method of manufacturing oxygenated fuel
US6660889B2 (en) 2000-03-27 2003-12-09 Toyota Jidosha Kabushiki Kaisha Method of manufacturing oxygenated fuel

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