Liquid-liquid dispersion and flow characteristics in a miniaturized annular rotating device

被引:19
|
作者
Wang, Yubin [1 ]
Tang, Tianyao [1 ]
Yan, Zifei [1 ]
Duan, Wuhua [2 ]
Deng, Jian [1 ]
Luo, Guangsheng [1 ]
机构
[1] Tsinghua Univ, Dept Chem Engn, State Key Lab Chem Engn, Beijing 100084, Peoples R China
[2] Tsinghua Univ, Inst Nucl & New Energy Technol, Collaborat Innovat Ctr Adv Nucl Energy Technol, Beijing 102201, Peoples R China
基金
中国国家自然科学基金;
关键词
Liquid-liquid dispersion; Miniaturized annular rotating device; Droplet diameter; Pressure drop; Liquid hold-up; EXTRACTION; BUBBLES; MIXER;
D O I
10.1016/j.cej.2022.140374
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Liquid-liquid microchemical processes suffer from the problems of small handling capacity and large pressure drops. In particular, process intensification is highly required for high phase ratios of the dispersion phase to the continuous phase and high-viscosity conditions. In this study, we reported a novel microdispersion device named miniaturized annular rotating device (m-ARD), which is a novel microdispersion device with a large handling capacity, small pressure drop, and relatively narrow droplet distribution, even at a low phase ratio of the continuous phase to the dispersion phase and under high-viscosity conditions. Various parameters were studied to determine the dispersion of the generated droplets and the flow pattern, average droplet diameter, pressure drop, and hold-up of the dispersion phase. Two typical droplet generation routes, namely, dripping and jetting, and typical flow patterns, i.e., helical and annular flows were also obtained. Transition maps of the droplet generation route and flow pattern were constructed. The average droplet diameter and handling capacity were up to 380 mu m and 30 mL/min, respectively. A small pressure drop was observed in the m-ARD. Furthermore, two dimensionless equations were developed to calculate the average droplet diameter and hold-up of the dispersion phase. This work provides a promising dispersion technology for the process intensification of liq-uid-liquid mass transfer and reactions.
引用
收藏
页数:10
相关论文
共 50 条
  • [1] Liquid-liquid flow and mass transfer characteristics in a miniaturized annular centrifugal device
    Wang, Yubin
    Du, Chencan
    Yan, Zhifei
    Duan, Wuhua
    Deng, Jian
    Luo, Guangsheng
    CHEMICAL ENGINEERING JOURNAL, 2022, 431
  • [2] Micro-dispersion, flow and mass transfer characteristics of high viscosity gas-liquid flow in a miniaturized annular rotating device
    Xu, Tao
    Wang, Guanglong
    Bai, Changyun
    Chen, Ming
    Li, Jun
    Wang, Yubin
    SEPARATION AND PURIFICATION TECHNOLOGY, 2025, 362
  • [4] CO2 capture in a miniaturized annular rotating device with countercurrent flow
    Wang, Yubin
    Yan, Zifei
    Deng, Jian
    Luo, Guangsheng
    SEPARATION AND PURIFICATION TECHNOLOGY, 2023, 317
  • [5] CFD modelling of mass transfer in liquid-liquid core-annular flow in a microchannel
    Singh, K. K.
    Chaurasiya, Rajnesh Kumar
    CHEMICAL ENGINEERING SCIENCE, 2022, 249
  • [6] Liquid-liquid two-phase flow and mass transfer characteristics in packed microchannels
    Su, Yuanhai
    Zhao, Yuchao
    Chen, Guangwen
    Yuan, Quan
    CHEMICAL ENGINEERING SCIENCE, 2010, 65 (13) : 3947 - 3956
  • [7] Drop velocity in a rotating liquid-liquid system
    Jammoal, Y.
    Lee, J. M. G.
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 2015, 104 : 638 - 646
  • [8] Zein nanoparticles produced by liquid-liquid dispersion
    Zhong, Qixin
    Jin, Minfeng
    FOOD HYDROCOLLOIDS, 2009, 23 (08) : 2380 - 2387
  • [9] TYPES OF DISPERSION IN AGITATED LIQUID-LIQUID SYSTEMS
    KATO, S
    NAKAYAMA, E
    KAWASAKI, J
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1991, 69 (01) : 222 - 227
  • [10] Mass transfer characteristics of liquid-liquid flow in small diameter conduits
    Biswas, Koushik Guha
    Das, Gargi
    Ray, Subhabrata
    Basu, Jayanta Kumar
    CHEMICAL ENGINEERING SCIENCE, 2015, 122 : 652 - 661