Abstract
The process of the sulfuric-acid alkylation of isoparaffins with olefins in a new-generation reaction apparatus, namely, the energy-efficient tubular contactor with diffuser–confuser design, which operates in the mode of jet agitation of raw material flows and a catalyst with the arrangement of internal cooling due to partial evaporation of isobutane, has made it possible to obtain high-octane hydrocarbon fractions with a content of 3-methylpentanes of up to 47 wt % and an octane number of up to 92. Energy efficiency has been achieved by eliminating the external cooling of the reaction mass, mechanical agitation, and additional pump-forced circulation equipment. The results of the industrial trials of the new contactor have been described.
Sign-in/Register to access full text options 
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Schedule a callDisclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.
