GB702224A - Improvements in or relating to the production of oxygen-containing organic compounds - Google Patents

Improvements in or relating to the production of oxygen-containing organic compounds

Info

Publication number
GB702224A
GB702224A GB5941/51A GB594151A GB702224A GB 702224 A GB702224 A GB 702224A GB 5941/51 A GB5941/51 A GB 5941/51A GB 594151 A GB594151 A GB 594151A GB 702224 A GB702224 A GB 702224A
Authority
GB
United Kingdom
Prior art keywords
liquid
withdrawn
olefines
point
reactor
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
GB5941/51A
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.)
Anglo Iranian Oil Co Ltd
Original Assignee
Anglo Iranian Oil Co Ltd
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 Anglo Iranian Oil Co Ltd filed Critical Anglo Iranian Oil Co Ltd
Priority to GB5941/51A priority Critical patent/GB702224A/en
Publication of GB702224A publication Critical patent/GB702224A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/49Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide
    • C07C45/50Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide by oxo-reactions

Landscapes

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

Abstract

In an OXO synthesis using a "cobalt carbonyl" catalyst part of the reaction mixture, consisting at least in part of liquid phase material, is withdrawn from a point remote from the point of entry of the reactants, cooled and returned without phase separation to the reactor at a point nearer to the point of entry of the reactants and at a temperature not less than the minimum required for the synthesis. The term "cobalt carbonyl" covers true carbonyls such as Co(CO)8 and carbonyl hydrides such as Co(CO)4H. Temperatures specified are 80-180 DEG C. Recycled material may be withdrawn and returned at a plurality of points. Cooling may be effected by heat exchangers. Preferably the recycling rate should be high, e.g. at a volume flow rate of 5-50 times the rate at which fresh feed is passed to the reactor. Preferably the Reynolds number of the liquid in the heat exchanger is 10,000-30,000. Preferably the temperature drop during circulation is relatively low, e.g. below 50 DEG C., preferably below 20 DEG C. Preferred inlet and outlet temperatures vary with the olefine used and a table is provided giving these temperatures for a number of olefines. The withdrawn stream may comprise gas and liquid or using upflow conditions through the reactor especially with C2-C4 olefines, liquid streams and gas streams are removed from different points and recombined before cooling. The liquid phase product stream may be combined with fresh CO and H2 before cooling. Olefine hydrocarbons are preferred feedstocks but olefines containing such groups as ester, halogen, aldehyde and acetal may also be used. Lower olefines, e.g. ethylene, propylene and butenes, are especially preferred. It is particularly preferred that cobalt catalysts are not introduced in the solid phase. Diagrams are provided of apparatus used when a single product stream is withdrawn and when separate gas and liquid streams are removed. Specifications 647,363, 702,191, 702,192, 702,195, 702,196, 702,197, 702,201, 702,203 and 702,204 are referred to.
GB5941/51A 1951-03-12 1951-03-12 Improvements in or relating to the production of oxygen-containing organic compounds Expired GB702224A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB5941/51A GB702224A (en) 1951-03-12 1951-03-12 Improvements in or relating to the production of oxygen-containing organic compounds

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB5941/51A GB702224A (en) 1951-03-12 1951-03-12 Improvements in or relating to the production of oxygen-containing organic compounds

Publications (1)

Publication Number Publication Date
GB702224A true GB702224A (en) 1954-01-13

Family

ID=9805494

Family Applications (1)

Application Number Title Priority Date Filing Date
GB5941/51A Expired GB702224A (en) 1951-03-12 1951-03-12 Improvements in or relating to the production of oxygen-containing organic compounds

Country Status (1)

Country Link
GB (1) GB702224A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2912464A (en) * 1957-10-04 1959-11-10 Union Carbide Corp Hydroformylation of conjugated dienes
US2995575A (en) * 1956-11-30 1961-08-08 Union Carbide Corp High pressure oxo conversion process

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2995575A (en) * 1956-11-30 1961-08-08 Union Carbide Corp High pressure oxo conversion process
US2912464A (en) * 1957-10-04 1959-11-10 Union Carbide Corp Hydroformylation of conjugated dienes

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