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- W2384169628 abstract "MIP(maximizing iso-paraffins process)process utilizes the technique of linking two reaction zones in series,and hence effectively improves gasoline quality.Cold simulation of MIP reactors can reveal the flow structures in the second reaction zone and also the effects of geometrical structures,but cannot provide the changes in hydrodynamics resulting from catalytic cracking reactions.To capture these changes,this work aimed at carrying out three-dimensional simulation of the MIP reactor by considering the reactions.The simulation was based on the two-fluid model and 12-lump kinetic model.The inter-phase momentum transfer and heat transfer models took into account the effects of multi-scale flow structures,and were compared with the traditional models based on homogeneous state.The simulation found that the multi-scale models could reasonably predict the flow structures and solids volume fraction in the second reaction zone as well as the temperature profiles,compared to the traditional model.For predicting product yields,both models showed similar results.They had good predictions in slurry and diesel,but fail to predict LPG and dry gas.The above finding implied that the effects of multi-scale structures should not only be considered in the momentum transfer and heat transfer models,but also be taken into account in the lumped kinetic model." @default.
- W2384169628 created "2016-06-24" @default.
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- W2384169628 date "2013-01-01" @default.
- W2384169628 modified "2023-09-26" @default.
- W2384169628 title "Numerical simulation of reaction process in MIP riser based on multi-scale model" @default.
- W2384169628 hasPublicationYear "2013" @default.
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