Abstract
AbstractA three‐phase bubbling fluidised bed model has been developed to simulate and predict the performance of a methane catalytic cracking fluidised bed reactor, using Ni/(porous and non‐porous) Al2O3 catalysts, under relevant conditions. The model includes the chemistry and hydrodynamics occurring within the fluidised bed reactor. Methane cracking kinetics, developed in a previous work using a thermo balance, was used in the model. The model predictions were compared to the results from an experimental study carried out in a lab‐scale fluidised bed. Good fit between experimental data and the model was obtained under a wide range of reaction conditions.
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.
