Abstract

A model for predicting conversions and yield patterns in FCC riser reactor is developed considering heat transfer, gas oil vaporization, catalyst entrainment hydrodynamics, mass transfer, catalytic cracking kinetics and deactivation. The effect of the initial average droplet size generated by feed atomization nozzle on conversion and yield pattern is discussed.

Full Text
Paper version not known

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 call