چکیده مقاله
Light olefins, especially ethylene and propylene, are essential intermediates in the petrochemical industry, which are used to produce polyethylene, polypropylene, and other essential products Olefins can be produced using different processes and raw materials The method of converting methanol to olefins is one of the processes that has received much attention in recent years The purpose of this research is to review the mathematical modeling of the reaction and regenerator sections, hydrodynamic simulation, heat transfer, and reaction in the fluidized bed reactor using computational fluid dynamics CFD , large eddy simulation LES , for methanol to olefin process MTO It is also an examination of effective parameters such as reactor length, reactor flow rate, product distribution, optimal product distribution scenario, and flow rates in a fluidized bed reactor
کلیدواژهها
نویسندگان
Mahdieh Garmsirian
Petroleum University of Technology, Ahwaz Faculty of Petroleum, Gas Engineering Department
Reza Mosayebbi behbahani
Petroleum University of Technology, Ahwaz Faculty of Petroleum, Gas Engineering Department
Moslem Fattahi
Petroleum University of Technology, Ahwaz Faculty of Petroleum, Gas Engineering Department
Mohammagreza Khosravi nikou
Petroleum University of Technology, Ahwaz Faculty of Petroleum, Gas Engineering Department
شیوه ارجاع
Garmsirian, Mahdieh and Mosayebbi behbahani, Reza and Fattahi, Moslem and Khosravi nikou, Mohammagreza,1402,Mathematical Modeling, Simulation of Reaction, and Regeneration Sections of MTO Process: Review,The second international congress of chemical engineering and oil industry,Tehran
ارائهشده در
مجموعه مقالات دومین کنگره بین المللی دانشجویان مهندسی شیمی و صنعت نفت30 آبان 1402 · تهران