Abstract

The steady state operation of a long tubular fixed-bed reactor in which a single highly exothermic reaction is occurring is analyzed. To avoid temperature runaways, such reactors must be operated so that their temperature rises $\Delta T$ are small fractions of the adiabatic temperature rise $\Delta T_{{\text{ad}}} $ . So here asymptotic methods based on $\Delta T/\Delta T_{{\text{ad}}} \ll 1$ are used to determine the radial temperature and concentration profiles. A simple one-dimensional (z only) reactor model is then derived by substituting these asymptotically correct radial profiles into the full two-dimensional reactor equations and then averaging in r. By comparing with numerical solutions of the two-dimensional reactor equations, it is found that the one-dimensional model accurately simulates the two-dimensional equations, even in the highly sensitive runaway region. It is also shown that a runaway criterion derived from the model accurately predicts the runaway transition of the original two-dime...

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

Disclaimer: 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.