Patent GB-836895-A (GB)
Title: Process for carrying out telomerisation reactions
IPC: C07C17/275
Filed: 1957-01-14
Abstract: In a process for the preparation of telomers of olefines such as ethylene, propylene, hexene, octene or styrene by reacting with telogens, such as carbon tetrachloride, chloroform, cyanogen chloride or aldehydes in the presence of free radical forming catalysts, the catalyst is sprayed, preferably through a nozzle in a finely-divided liquid form or as a solution in an inert solvent, or as a solution or suspension in the telogen into the gaseous or liquid reaction mixture.  Elevated temperatures and pressures, e.g. up to 250 DEG  C. and between 20 and 1000 atmospheres respectively, may be used and the process may be continuous or intermittent.  The catalysts may be, e.g., organic peroxides, azobutyric nitrile, redox systems or hydrogen peroxide.  In examples (1) to (4) a mixture of azo-isobutyric acid nitrile catalyst and cyanogen chloride is sprayed into ethylene under pressure, fresh ethylene constantly added and the resulting telomer separated by vacuum distillation to form an undistillable fraction and a distillate which is vacuum rectified to yield in Example 1, b -chloropropionic, d -chloro-n-valeronitrile, o -chloro - n - enanthic, w - chloro - n - pelargonic, w - chloro - n - undecanic acid nitriles and higher compounds.  In Example (5), carbon tetrachloride containing benzoyl peroxide catalyst is sprayed into ethylene to yield, 1,1,1,3-tetrachloropropane, 1,1,1,5-tetrachloropentane, 1,1,1,7 - tetrachloroheptane, 1,1,1,7 - tetrachlorononane and above; and in Examples (6) and (7) carbon tetrachloride containing azoisobutyric acid nitrile yields C3 to C9 fractions.  Specifications 836,896 and 836,897 are referred to.ALSO:In a process for the preparation of telomers of olefines such as ethylene, propylene, hexene, octene, or styrene by reacting with telogens such as carbon tetrachloride, chloroform, cyanogen chloride or aldehydes in the presence of freeradical forming catalysts, the catalyst is sprayed preferably through a nozzle in a finely divided liquid form or as a solution in an inert solvent or as a solution or suspension in the telogen into the gaseous or liquid reaction mixture.  Elevated temperatures and pressures e.g. up to 250 DEG  C. and between 20 and 1000 atmospheres respectively may be used and the process may be continuous or intermittent.  The catalysts e.g. organic peroxides, azo-butyric nitrile, redox systems or hydrogen peroxide may be added in admixture with the reactants or in solution in an inert solvent. In examples: (1) to (4) a mixture of azo-isobutyric acid nitrile catalyst and cyanogen chloride is sprayed into ethylene under pressure and fresh ethylene constantly added and the resulting telomer separated by vacuum distillation to form an undistillable fraction and a distillate which is vacuum rectified to yield, in Example 1, B. chloropropionic d -chloro-n-valeronitrile, o -chloro-n-enanthic, o -chloro - n - pelargonic, o  - chloro - n - undecanic acid nitriles and higher compounds.  In Example (5) carbon tetrachloride containing benzoyl peroxide catalyst is sprayed into ethylene to yield after vacuum fractionation 1,1,1,3-tetrachloropropane, 1,1,1,5 - tetrachloropentane 1,1,1,7 - tetrachloroheptane, 1,1,1,7-tetrachlorononane and above; and in Examples (6) and (7) carbon tetrachloride containing azoisobutyric acid nitrile yield C3-C9 fractions. Specifications 836,896 and 836,897 are referred to.