(756h) Olefin Oligomerization on Acidic Zeolites: A Mechanistic Model for Catalyst Optimization
AIChE Annual Meeting
2020
2020 Virtual AIChE Annual Meeting
Catalysis and Reaction Engineering Division
Hydrocarbon Conversion III: Hydrocarbon Transformation
Thursday, November 19, 2020 - 9:45am to 10:00am
A reaction network consisting of 3705 surface reactions and 538 physisorption/desorption steps and involving 909 molecular and ionic species was automatically constructed by using a network generator [1]. The frequency factors were computed in the framework of transition state theory and the activation energies were expressed as functions of the heats of reaction in the physisorbed state, which were calculated from thermodynamic considerations [2].
The model demonstrated that increasing the stabilization enthalpy of the ionic intermediates drives the selectivity of the process toward the production of C9 species. This would result into a more efficient oligomerization process whose target is the production of gasoline blend with high concentration of heavy and highly branched olefins and, as a consequence, with high octane number. This study revealed mechanistic details of acid-catalyzed oligomerization chemistry of light olefins. The developed microkinetic model represents a powerful tool to predict the product distribution, optimize the conditions of the process and design more efficient catalysts.
References
[1] Vernuccio, S. and Broadbelt, L. J., âDiscerning complex reaction networks using automated generatorsâ. AIChE J. 65, e16663 (2019).
[2] Vernuccio, S., Bickel, E. E., Gounder, R., Broadbelt L. J., âMicrokinetic model of propylene oligomerization on Brønsted acidic zeolites at low conversionâ. ACS Catal. 9, pp. 8996â9008 (2019).