Modeling and Kinetic Study of the Transformation of C6- Paraffins Over Methanol to Olefin Catalyst, M.Sc. Thesis Sharif University of Technology ; Kazemeini, Mohammad (Supervisor) ; Mohammad Rezaie, Alireza (Co-Advisor)
Abstract
Catalytic cracking of iso and normal butane over HZSM-5 at several temperatures and a variety of contact time and different partial pressures of hydrocarbon feed was conducted. Experiments indicate that the operating conditions have considerable effects on final product distribution and feed conversion. Results show that high temperatures, low contact time and partial pressure of paraffin feed favor the light olefin production, particularly propylene production. Results obtained for iso-butane show a similar conversion values in comparison to n-butane but a higher olefin and propylene selectivity. Finally kinetic modeling of both iso and normal butane cracking was performed based on a lump...
Cataloging briefModeling and Kinetic Study of the Transformation of C6- Paraffins Over Methanol to Olefin Catalyst, M.Sc. Thesis Sharif University of Technology ; Kazemeini, Mohammad (Supervisor) ; Mohammad Rezaie, Alireza (Co-Advisor)
Abstract
Catalytic cracking of iso and normal butane over HZSM-5 at several temperatures and a variety of contact time and different partial pressures of hydrocarbon feed was conducted. Experiments indicate that the operating conditions have considerable effects on final product distribution and feed conversion. Results show that high temperatures, low contact time and partial pressure of paraffin feed favor the light olefin production, particularly propylene production. Results obtained for iso-butane show a similar conversion values in comparison to n-butane but a higher olefin and propylene selectivity. Finally kinetic modeling of both iso and normal butane cracking was performed based on a lump...
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