Hydrochloric Acid → tert-BUTYL CHLORIDE

A continuous process for preparing low molecular weight polyisobutylene having an Mn in the range of 700 to 3,000 and a molecular weight distribution less than about 2.0 from a feedstream mixture of C4 hydrocarbons containing at least about 6% by weight isobutylene in a continuous stirred reactor maintained at a reaction temperature of about -50° to +30° C., the reactor having a feedstream inlet and a separate AlCl3 catalyst inlet, which comprises injecting gaseous HCl, in an amount of 25 to 200 ppm parts by weight of feedstream and in the absence of AlCl3, into said feedstream at a point prior to its entry into the reactor in a manner sufficient to permit substantially complete reaction of the HCl with isobutylene to form t-butyl chloride before contact with AlCl3 such that the resulting pre-reacted feedstream at the point of reactor entry contains less than 1.0 ppm HCl, and simultaneously adding the pre-reacted feedstream and the AlCl3 catalyst to the reactor and contacting the pre-reacted feedstream with said catalyst in the reaction mixture to form the polyisobutylene, withdrawing the reaction mixture from the reactor, quenching the reaction with aqueous alkali and separating therefrom the polyisobutylene product.

1. temperaturemaintained at a reaction temperature of about -50° to +30° C.

ORD record

ord-9f7d5ad5fa654d8b87f44d7ae12db54f

Source dataset

uspto-grants-1985_12

DOI

10.6084/m9.figshare.5104873.v1

Patent number

US04558170