CFD simulation of flow and mixing characteristics in a stirred tank agitated by improved disc turbines

被引:17
|
作者
Jia, Zhuotai [1 ,2 ]
Xu, Lele [3 ]
Duan, Xiaoxia [1 ]
Mao, Zai-Sha [1 ]
Zhang, Qinghua [1 ,2 ]
Yang, Chao [1 ,2 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, CAS Key Lab Green Proc & Engn, Beijing 100190, Peoples R China
[2] Univ Chinese Acad Sci, Sch Chem Engn, Beijing 100049, Peoples R China
[3] Nanjing Tech Univ, Sch Chem Engn, Nanjing 211816, Peoples R China
来源
CHINESE JOURNAL OF CHEMICAL ENGINEERING | 2022年 / 50卷
基金
中国国家自然科学基金;
关键词
Flow regime; Mixing time; Stirred vessel; Computational fluid dynamics; Improved disc turbine; RUSHTON-TURBINE; POWER-CONSUMPTION; TURBULENCE MODELS; GAS-LIQUID; IMPELLER; ENERGY; BLADE; PATTERNS;
D O I
10.1016/j.cjche.2022.05.017
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
To reduce the power consumption and improve the mixing performance in stirred tanks, two improved disc turbines namely swept-back parabolic disc turbine (SPDT) and staggered fan-shaped parabolic disc turbine (SFPDT) are developed. After validation of computational fluid dynamics (CFD) model with experimental results, CFD simulations are carried out to study the flow pattern, mean velocity, power consumption, pumping capacity and mixing efficiency of the improved and traditional impellers in a dished-bottom tank under turbulent flow conditions. The results indicate that compared with the commonly used parabolic disc turbine (PDT), the power number of proposed SPDT and SFPDT impellers is reduced by 43% and 12%, and the pumping efficiency is increased by 68% and 13%, respectively. Furthermore, under the same power consumption (0-700 W center dot m(-3)), the mixing performance of both SPDT and SFPDT is also superior to that of Rushton turbine and PDT. (c) 2022 The Chemical Industry and Engineering Society of China, and Chemical Industry Press Co., Ltd. All rights reserved.
引用
收藏
页码:95 / 107
页数:13
相关论文
共 50 条
  • [1] CFD simulation of flow and mixing characteristics in a stirred tank agitated by improved disc turbines
    Zhuotai Jia
    Lele Xu
    Xiaoxia Duan
    Zai-Sha Mao
    Qinghua Zhang
    Chao Yang
    ChineseJournalofChemicalEngineering, 2022, 50 (10) : 95 - 107
  • [2] CFD SIMULATION OF THE HYDRODYNAMICS AND MIXING TIME IN A STIRRED TANK
    Ochieng, Aoyi
    Onyango, Maurice S.
    CHEMICAL INDUSTRY & CHEMICAL ENGINEERING QUARTERLY, 2010, 16 (04) : 379 - 386
  • [3] CFD simulation of local and global mixing time in an agitated tank
    Liangchao Li
    Bin Xu
    Chinese Journal of Mechanical Engineering, 2017, 30 : 118 - 126
  • [4] CFD Simulation of Local and Global Mixing Time in an Agitated Tank
    LI Liangchao
    XU Bin
    Chinese Journal of Mechanical Engineering, 2017, 30 (01) : 118 - 126
  • [5] CFD simulation of local and global mixing time in an agitated tank
    Li Liangchao
    Xu Bin
    CHINESE JOURNAL OF MECHANICAL ENGINEERING, 2017, 30 (01) : 118 - 126
  • [6] CFD simulation of mixing in a stirred tank with multiple hydrofoil impellers
    Min, J
    Gao, ZM
    Shi, LT
    CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2005, 13 (05) : 583 - 588
  • [7] CFD Simulation of Mixing in a Stirred Tank with Multiple Hydrofoil Impellers
    闵健
    高正明
    施力田
    Chinese Journal of Chemical Engineering, 2005, (05) : 13 - 18
  • [8] CFD Simulation of Gas Dispersion in a Stirred Tank of Dual Rushton Turbines
    Li, Xinju
    Guan, Xiaoping
    Zhou, Rongtao
    Yang, Ning
    Liu, Mingyan
    INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2017, 15 (04)
  • [9] The simplest stirred tank for laminar mixing: Mixing in a vessel agitated by an off-centered angled disc
    Bulnes-Abundis, D.
    Alvarez, M. M.
    AICHE JOURNAL, 2013, 59 (08) : 3092 - 3108
  • [10] Laminar Mixing in Stirred Tank Agitated by an Impeller Inclined
    Takahashi, Koji
    Sugo, Yoshiharu
    Takahata, Ysuyuki
    Sekine, Hitoshi
    Nakamura, Masayuki
    INTERNATIONAL JOURNAL OF CHEMICAL ENGINEERING, 2012, 2012