Numerical exploration of the flow regime transition of a novel catalytic cracking reactor and operation mode analysis-Reference-Cited by-同舟云学术

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Numerical exploration of the flow regime transition of a novel catalytic cracking reactor and operation mode analysis

Published:2022-01 Issue: Volume:398 Page:117137
ISSN:0032-5910
Container-title:Powder Technology
language:en
Short-container-title:Powder Technology

Author:

Han Caixia,Xu Youhao,Lu Bona,Wu Hao,Wang Wei

Funder

Chinese Academy of Sciences

National Natural Science Foundation of China

Publisher

Elsevier BV

Subject

General Chemical Engineering

Reference47 articles.

1. A novel fluid catalytic cracking process for maximizing iso-paraffins: from fundamentals to commercialization;Xu;Front. Chem. Sci. Eng.,2018

2. Flexibility of MIP technology;Tang;China Petrol. Process. Petrochem. Technol.,2015

3. A modified FCC process MIP for maximizing Iso-paraffins in cracked naphtha;Xu;Pet. Process. Petrochem.,2001

4. Development and commercial application of FCC process for maximizing Iso-Paraffins(MIP) in cracked naphtha;Xu;Eng. Sci.,2003

5. Diameter-Transformed Fluidized Bed;Xu,2020

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1. Regulating the crude oil–to–chemical process in a multizone fluidized bed reactor using unconventional catalyst formulations;Powder Technology;2024-04

2. Hydrodynamic Full-Loop Simulation of an Industrial Fluid Catalytic Cracking Fluidized Bed System with Mechanical Valves;Industrial & Engineering Chemistry Research;2024-02-07

3. Role of mesoscale structure in gas–solid fluidization: Comparison between continuum and discrete approaches;Chemical Engineering Journal;2023-02

4. Two‐Phase and Three‐Phase Modeling of an Industrial Fluidized Bed for Maximizing Iso‐Paraffins;Chemie Ingenieur Technik;2022-12-03

5. Multiscale CFD Simulation of an Industrial Diameter-Transformed Fluidized Bed Reactor with Artificial Neural Network Analysis of EMMS Drag Markers;Industrial & Engineering Chemistry Research;2022-06-09

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