CIESC Journal ›› 2013, Vol. 64 ›› Issue (6): 2065-2071.DOI: 10.3969/j.issn.0438-1157.2013.06.023

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Model prediction for particles circulation flux ratio in coupled reactor with riser and gas-solids loop fluidized bed

WANG Dewu1,2, YAN Chaoyu2, LU Chunxi2, ZHANG Shaofeng1,3   

  1. 1. School of Chemical Engineering and Technology, Hebei University of Technology, Tianjin 300130, China;
    2. State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, China;
    3. Engineering Research Center of Seawater Utilization Technology of Ministry of Education, Hebei University of Technology, Tianjin 300130, China
  • Received:2012-11-27 Revised:2013-01-09 Online:2013-06-05 Published:2013-06-05
  • Supported by:

    supported by the National Natural Science Foundation of China(21106028,20976190)and the Natural Science Foundation of Hebei Province(B2013202125).

提升管与气-固环流床层耦合反应器颗粒相循环比的模型及预测

王德武1,2, 严超宇2, 卢春喜2, 张少峰1,3   

  1. 1. 河北工业大学化工学院,天津 300130;
    2. 中国石油大学(北京)重质油国家重点实验室,北京 102249;
    3. 河北工业大学海水资源高效利用化工技术教育部工程研究中心,天津 300130
  • 通讯作者: 卢春喜
  • 作者简介:王德武(1980—),男,博士,副教授。
  • 基金资助:

    国家自然科学基金项目(21106028,20976190);河北省自然科学基金项目(B2013202125)。

Abstract: A mathematical model predicting particles flux ratio between internal circulation and external circulation processed in a coupled reactor with gas-solids loop fluidized bed was established.In a wide range of operating conditions, particles circulation flux ratio was predicted, and the particles circulation ratio np=20 was determined as a criterion to analyze the particles mixing behavior in internal and external loops.The results showed that the calculated values basically agreed with experimental data, and the average relative error approached 15.35%.Particles circulation ratio increased with increasing superficial gas velocity in the draft tube, however decreased with increasing particles external circulation flux and opening rate of a lotus-shaped distributor, with the change in two stages, first fast and then slow.The transition points were Ug,d=0.50 m·s-1, Gs,r=110 kg·m-2·s-1, and α=10% respectively.Under the operating conditions of riser superficial gas velocity Ug,r=10—21.17 m·s-1, draft tube superficial gas velocity Ug,d=0.57—1.50 m·s-1, particles external circulation flux Gs,r ≥110 kg·m-2·s-1, and distributor open rate α≥10%, the particles complete mixing status in the riser and the gas-solids loop bed reactor could be avoided.

Key words: riser, gas-solids loop fluidized bed, coupled reactor, mixing, ratio of particle circulation flux, internal circulation, external circulation

关键词: 提升管, 气-固环流床层, 耦合反应器, 混合, 颗粒相循环比, 内循环, 外循环

CLC Number: