Experimental investigation of hydrodynamics and suspension characteristics in a boiling stirred tank reactor with helical coils

被引:0
|
作者
Zhou, Feng [1 ,2 ]
Wang, Taoran [1 ,2 ]
Cai, Jinjin [1 ,2 ]
Mao, Xiaoning [1 ,2 ]
Wu, Zhenyu [1 ,2 ]
Nie, Yong [1 ,2 ]
机构
[1] Zhejiang Univ Technol, Biodiesel Engn Lab China Petr & Chem Ind Federat, Hangzhou 310014, Zhejiang, Peoples R China
[2] Zhejiang Univ Technol, Zhejiang Prov Key Lab Biofuel, Hangzhou 310014, Zhejiang, Peoples R China
关键词
Boiling stirred tank; Gas-liquid-solid; Hydrodynamics; Solids suspension; Power consumption; CRITICAL IMPELLER SPEED; SOLID SUSPENSION; POWER-CONSUMPTION; CFD SIMULATIONS; MASS-TRANSFER; LIQUID; DISPERSION; FLOW; PREDICTION; PARTICLES;
D O I
10.1016/j.powtec.2024.120118
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The boiling stirred tank reactor (BSTR) is widely used in the chemical industry, while the relevant basic data of hydrodynamics and suspension characteristics for reactor design are quite limited. In this work, the hydrodynamics and suspension characteristics in a BSTR with helical coils (BSTR@HC) were studied using three types of impellers. Particle image velocimetry and visualization experiments reveal different flow fields and nucleation processes of three impellers. Suspension experiments show that superficial vapor velocity, solid loading, and particle size play an important role for just-suspension impeller speed Njsvand power consumption Pjsv,while cloud height is mainly determined by superficial vapor velocity. Among the three impellers, radial impeller shows the best suspension performance in BSTR@HC. Correlations of Njsvand Pjsvwere developed with relative mean deviations of 2.7% and 4.6%, respectively. Furthermore, a model for the estimation of energy efficiency was developed by evaluate specific power consumption epsilon jsv.
引用
收藏
页数:14
相关论文
共 50 条
  • [1] An experimental investigation into vapor dispersion and solid suspension in boiling stirred tank reactors
    Dohi, N
    Matsuda, Y
    Shimizu, K
    Minekawa, K
    Kawase, Y
    [J]. CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2002, 41 (03) : 267 - 279
  • [2] Hydrodynamics in a horizontal stirred tank reactor
    van der Gulik, GJS
    Wijers, JG
    Keurentjes, JTF
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2001, 40 (03) : 785 - 794
  • [3] Experimental investigation of subcooled flow boiling heat transfer in helical coils
    Chen, Shuo
    Hu, Zhenxiao
    Xiao, Yao
    Gu, Hanyang
    [J]. NUCLEAR ENGINEERING AND DESIGN, 2018, 327 : 187 - 197
  • [4] Suspension and flow dynamics of the AllegroTM stirred tank reactor
    Delbridge, J. N.
    Barrett, T. A.
    Ducci, A.
    Micheletti, M.
    [J]. CHEMICAL ENGINEERING RESEARCH & DESIGN, 2023, 195 : 355 - 369
  • [5] Solid suspension in a boiling stirred tank with radial flow turbines
    Bao, Yuyun
    Gao, Zhengming
    Li, Zhipeng
    Bai, Ding
    Smith, John M.
    Thorpe, Rex B.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (07) : 2420 - 2427
  • [6] LIMITATION OF STIRRED TANK REACTOR AS EXPERIMENTAL CATALYTIC REACTOR
    MERLINO, D
    VONDERBE.CH
    [J]. ANALES DE QUIMICA-INTERNATIONAL EDITION, 1971, 67 (11): : 1103 - &
  • [7] Modeling and experimental study of a stirred tank reactor
    Dhainaut, M
    Tetlie, P
    Bech, K
    [J]. INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2005, 3
  • [8] Obtaining the Nusselt Equation with the Use of CFD for a Stirred Tank Heated with Helical Coils
    Jaimes, Ronald
    Nunhez, Jose R.
    [J]. ICHEAP12: 12TH INTERNATIONAL CONFERENCE ON CHEMICAL & PROCESS ENGINEERING, 2015, 43 : 1687 - 1692
  • [9] CFD Modeling of gas-liquid hydrodynamics in a stirred tank reactor
    Gorii, Mahmoud
    Bozorgmehry, Bozzarjomehry Ramin
    Kazemeini, Mohammad
    [J]. IRANIAN JOURNAL OF CHEMISTRY & CHEMICAL ENGINEERING-INTERNATIONAL ENGLISH EDITION, 2007, 26 (02): : 85 - 96
  • [10] CFD Simulation of the Fluid Hydrodynamics in a Continuous Stirred-Tank Reactor
    Zhang, Shuo
    Mueller, David
    Arellano-Garcia, Harvey
    Wozny, Guenter
    [J]. ICHEAP-11: 11TH INTERNATIONAL CONFERENCE ON CHEMICAL AND PROCESS ENGINEERING, PTS 1-4, 2013, 32 : 1441 - 1446