Improved steam utilisation with internals in the reactor section of fluid cokers

被引:0
|
作者
Wang, Ruixu [1 ]
Mezo, Andrew [1 ]
Wormsbecker, Michael [2 ]
Wiens, Jason [2 ]
机构
[1] Coanda Res & Dev Corp, 101-5140 North Fraser Way, Burnaby, BC V5J 0J4, Canada
[2] Syncrude Canada Ltd, 9421 17 Ave NW, Edmonton, AB T6N 1H4, Canada
关键词
Circulating fluidized bed; Fluid cokers; Baffles; Steam stripping; Helium gas tracer; GAS; BED; HYDRODYNAMICS; JET;
D O I
10.1016/j.powtec.2023.119138
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Gas tracer experiments were carried out in a cold flow model that is geometrically and dynamically scaled down from commercial fluid cokers at a one ninth scale. Continuous helium tracer injections were made into the attrition and stripping gas spargers to observe the gas-solids mixing in the dense bed. Helium concentration profiles, which represent steam in the commercial reactor, were measured with different baffle configurations. The experiments demonstrate the annular region of the dense bed was helium-lean without any internals, meaning stripping is poor at the vessel walls, whereas the addition of internals promotes dense bed stripping in the proximity of the internal. Improved steam distribution implies better stripping performance, which leads to increased reactor product yield.
引用
收藏
页数:18
相关论文
共 50 条
  • [31] Modeling and Optimization of Ethane Steam Cracking Process in An Industrial Tubular Reactor with Improved Reaction Scheme
    Mohsin Ali
    Liao Zuwei
    Yao Yang
    Sun Jingyuan
    Jiang Binbo
    Wang Jingdai
    Yang Yongrong
    China Petroleum Processing & Petrochemical Technology, 2020, 22 (04) : 117 - 125
  • [32] Modeling and Optimization of Ethane Steam Cracking Process in An Industrial Tubular Reactor with Improved Reaction Scheme
    Ali, Mohsin
    Liao Zuwei
    Yang, Yao
    Sun Jingyuan
    Jiang Binbo
    Wang Jingdai
    Yang Yongrong
    CHINA PETROLEUM PROCESSING & PETROCHEMICAL TECHNOLOGY, 2020, 22 (04) : 117 - 125
  • [33] Improved catalytic performance of Ni catalysts for steam methane reforming in a micro-channel reactor
    Bozhao Chu
    Nian Zhang
    Xuli Zhai
    Xin Chen
    Yi Cheng
    Journal of Energy Chemistry, 2014, 23 (05) : 593 - 600
  • [34] Improved catalytic performance of Ni catalysts for steam methane reforming in a micro-channel reactor
    Bozhao Chu
    Nian Zhang
    Xuli Zhai
    Xin Chen
    Yi Cheng
    Journal of Energy Chemistry, 2014, (05) : 593 - 600
  • [35] Improved catalytic performance of Ni catalysts for steam methane reforming in a micro-channel reactor
    Chu, Bozhao
    Zhang, Nian
    Zhai, Xuli
    Chen, Xin
    Cheng, Yi
    JOURNAL OF ENERGY CHEMISTRY, 2014, 23 (05) : 593 - 600
  • [36] Improved Computational Fluid Dynamics Framework for Reactor Core Baffle Swelling Assessment
    Filonova, Yuliia
    Dubyk, Yaroslav
    Filonov, Vladislav
    Kondratjuk, Vadym
    JOURNAL OF NUCLEAR ENGINEERING AND RADIATION SCIENCE, 2021, 7 (01):
  • [37] 1D Model for Coupled Simulation of Steam Cracker Convection Section with Improved Evaporation Model
    Verhees, Pieter
    Amghizar, Ismael
    Goemare, Juhl
    Akhras, Abdul Rahman
    Marin, Guy B.
    Van Geem, Kevin M.
    Heynderickx, Geraldine J.
    CHEMIE INGENIEUR TECHNIK, 2016, 88 (11) : 1650 - 1664
  • [38] Mathematical modeling of hydrogen production using methanol steam reforming in the coupled membrane reactor when the output materials of the reformer section is used as feed for the combustion section
    Talaghat, Mohammad Reza
    Naamaki, Nourollah
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2021, 46 (02) : 2282 - 2295
  • [39] Computational fluid dynamics study on concentration polarization phenomena in silica membrane reactor during methanol steam reforming
    Seiiedhoseiny, M.
    Ghasemzadeh, K.
    Jalilnejad, E.
    Iulianelli, A.
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2023, 183
  • [40] Effects of Ca-Based Catalysts on Biomass Gasification with Steam in a Circulating Spout-Fluid Bed Reactor
    Xie, Yurong
    Xiao, Jun
    Shen, Laihong
    Wang, Jun
    Zhu, Jing
    Mao, Jiangang
    ENERGY & FUELS, 2010, 24 (05) : 3256 - 3261