GB645086A - Aliphatic olefins and cyclic process for manufacture thereof - Google Patents

Aliphatic olefins and cyclic process for manufacture thereof

Info

Publication number
GB645086A
GB645086A GB8559/48A GB855948A GB645086A GB 645086 A GB645086 A GB 645086A GB 8559/48 A GB8559/48 A GB 8559/48A GB 855948 A GB855948 A GB 855948A GB 645086 A GB645086 A GB 645086A
Authority
GB
United Kingdom
Prior art keywords
saturated hydrocarbons
lighter
olefins
fraction
polymerization zone
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
GB8559/48A
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.)
California Research LLC
Original Assignee
California Research LLC
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 California Research LLC filed Critical California Research LLC
Publication of GB645086A publication Critical patent/GB645086A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2/00Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • C07C2/02Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons
    • C07C2/04Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation
    • C07C2/06Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation of alkenes, i.e. acyclic hydrocarbons having only one carbon-to-carbon double bond
    • C07C2/08Catalytic processes
    • C07C2/14Catalytic processes with inorganic acids; with salts or anhydrides of acids
    • C07C2/18Acids of phosphorus; Salts thereof; Phosphorus oxides
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2527/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • C07C2527/14Phosphorus; Compounds thereof
    • C07C2527/16Phosphorus; Compounds thereof containing oxygen
    • C07C2527/167Phosphates or other compounds comprising the anion (PnO3n+1)(n+2)-
    • C07C2527/173Phosphoric acid or other acids with the formula Hn+2PnO3n+1

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

In the preparation of polymeric olefins boiling above about 325 DEG F. and below about 520 DEG F. by contacting propylene with an acid polymerization catalyst in a polymerization zone, separating a lighter olefinic fraction boiling below said polymeric olefins, recycling said lighter fraction to the polymerization zone, and recovering said polymeric olefins boiling above 325 DEG F., decline in conversion rate to said higher boiling polymers is inhibited by rejecting a fraction comprising saturated hydrocarbons formed in said polymerization zone. Saturated hydrocarbons may be removed from the entire product or part thereof, such as the recycle stream. Thus part of said stream may be bled out. More selectively, saturated hydrocarbons are removed by liquid phase solvent extraction or unsaturated hydrocarbons are separated from them by adsorption on silica gel or the like. Alternatively, C5 and lighter saturated hydrocarbons are removed by fractionating the product, and C6 and above are recycled and suppress additional formation thereof. Part of the C5 may be recycled also. Preferably the process is applied to the interpolymerization of propylene with an acyclic C6 to C11 olefin with a phosphoric acid catalyst as in Specification 638,514, and operating conditions are otherwise as described in the said Specification as is the conversion of the olefins to alkyl sulphonates, alcohols, phenyl alkanes and alkyl phenols. Diolefins may be eliminated before conversion to monophenyl alkanes by silica gel adsorption or the mixture used to form mono- and di-phenyl alkanes which are then separated by distillation. Results of measurements of infra-red absorption which indicate the structure of the polypropylene products are given.
GB8559/48A 1947-04-05 1948-03-23 Aliphatic olefins and cyclic process for manufacture thereof Expired GB645086A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US645086XA 1947-04-05 1947-04-05

Publications (1)

Publication Number Publication Date
GB645086A true GB645086A (en) 1950-10-25

Family

ID=22056462

Family Applications (1)

Application Number Title Priority Date Filing Date
GB8559/48A Expired GB645086A (en) 1947-04-05 1948-03-23 Aliphatic olefins and cyclic process for manufacture thereof

Country Status (1)

Country Link
GB (1) GB645086A (en)

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