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- W2384667941 abstract "The two-phase model was employed to simulate the fluidized bed reactor for the continuous methanol to olefins(MTO) process over SAPO-34 catalyst.Followed by Lagrangian method,the MTO reactions and the coke accumulation on the SAPO-34 catalyst particles were investigated in detail,including the effects of the mass transfer rate,the catalyst residence time and the back-mixing of the catalyst particles on the MTO process.The results show that,the rate of the inter-phase mass transfer is much slower than the rate of the MTO chemical reaction,and the mass transfer is the controlling step in the fluidized bed MTO process.Increasing mass transfer rate or catalyst residence time,the coke accumulation on the catalyst will be promoted,which will also result in increasing the selectivity of ethylene and propylene.However,reducing the catalyst back-mixing or employing the multi-stage bed,the olefins products' distribution is affected only a little.And the option of counter-current multi-stage bed even leads to a remarkable decrease of the selectivity of ethylene and propylene." @default.
- W2384667941 created "2016-06-24" @default.
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- W2384667941 date "2012-01-01" @default.
- W2384667941 modified "2023-09-24" @default.
- W2384667941 title "Simulation of Fluidized Bed Reactor for Methanol to Olefins (MTO) Process" @default.
- W2384667941 hasPublicationYear "2012" @default.
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