Measurements of the effective mass transfer areas for the gas-liquid rotating packed bed

被引:5
|
作者
Tian, Wen [1 ]
Ji, Junyi [1 ]
Li, Hongjiao [1 ]
Liu, Changjun [1 ,2 ]
Song, Lei [1 ]
Ma, Kui [1 ]
Tang, Siyang [1 ]
Zhong, Shan [1 ]
Yue, Hairong [1 ,2 ]
Liang, Bin [1 ,2 ]
机构
[1] Sichuan Univ, Sch Chem Engn, Low Carbon Technol & Chem React Engn Lab, Chengdu 610065, Peoples R China
[2] Sichuan Univ, Inst New Energy & Low Carbon Technol, Chengdu 610207, Peoples R China
关键词
Gas-liquid; Chemical absorption; Mass transfer areas; Rotating packed bed (RPB); PROCESS INTENSIFICATION; FLOW; PACKING; ABSORPTION; DISPERSION; SIMULATION; HOLDUP;
D O I
10.1016/j.cjche.2022.06.002
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Rotating packed bed (RPB) is one of the most effective gas-liquid mass transfer enhancement reactors, its effective specific mass transfer area (ae) is critical to understand the mass transfer process. By using the NaOH-CO2 chemical absorption method, the ae values of three RPB reactors with different rotor sizes were measured under different operation conditions. The results showed that the high gravity factor and liquid flow rate were major affecting factors, while the gas flow rate exhibited minor influence. The radius of packing is the dominant equipment factor to affect ae value. The results indicated that the contact area depends on the dispersion of the liquid phase, thus the centrifugal force of rotating packed bed greatly influenced the ae value. Moreover, the measured ae/ap (effective specific mass transfer area/specific surface area of packing) values were fitted with dimensionless correlation formulas. The unified correlation formula with dimensionless bed size parameter can well predict the experimental data and the prediction errors were within 15%.(c) 2022 The Chemical Industry and Engineering Society of China, and Chemical Industry Press Co., Ltd.
引用
收藏
页码:13 / 19
页数:7
相关论文
共 50 条
  • [1] Measurements of the effective mass transfer areas for the gas–liquid rotating packed bed
    Wen Tian
    Junyi Ji
    Hongjiao Li
    Changjun Liu
    Lei Song
    Kui Ma
    Siyang Tang
    Shan Zhong
    Hairong Yue
    Bin Liang
    ChineseJournalofChemicalEngineering, 2023, 55 (03) : 13 - 19
  • [2] CFD modeling of gas-liquid mass transfer process in a rotating packed bed
    Yang, Yucheng
    Xiang, Yang
    Chu, Guangwen
    Zou, Haikui
    Sun, Baochang
    Arowo, Moses
    Chen, Jian-Feng
    CHEMICAL ENGINEERING JOURNAL, 2016, 294 : 111 - 121
  • [3] Gas-Liquid Effective Interfacial Area in a Rotating Packed Bed
    Luo, Yong
    Chu, Guang-Wen
    Zou, Hai-Kui
    Zhao, Zhi-Qiang
    Dudukovic, Milorad P.
    Chen, Jian-Feng
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (50) : 16320 - 16325
  • [4] Influence of Gas-Liquid Distribution Inducer on Mass Transfer Coefficient in Rotating Packed Bed
    Wu, Fei
    Wu, Jie
    Jin, Mei
    Wang, Fang
    Lu, Ping
    MATERIALS SCIENCE, ENVIRONMENT PROTECTION AND APPLIED RESEARCH, 2014, 908 : 277 - 281
  • [5] Numerical simulation of gas-liquid two-phase flow and mass transfer in a rotating packed bed
    Xu, Ming
    Zhang, Jian-Wen
    Shen, Zhi-Gang
    Chen, Jian-Feng
    Zhao, Jin
    Beijing Huagong Daxue Xuebao (Ziran Kexueban)/Journal of Beijing University of Chemical Technology (Natural Science Edition), 2004, 31 (05):
  • [6] A Review on Gas-Liquid Mass Transfer Coefficients in Packed-Bed Columns
    Flagiello, Domenico
    Parisi, Arianna
    Lancia, Amedeo
    Di Natale, Francesco
    CHEMENGINEERING, 2021, 5 (03)
  • [7] Automated measurements of gas-liquid mass transfer in micropacked bed reactors
    Zhang, Jisong
    Teixeira, Andrew R.
    Jensen, Klavs F.
    AICHE JOURNAL, 2018, 64 (02) : 564 - 570
  • [8] Gas-liquid mass transfer in a rotating liquid redistributor
    Hacking, J. A.
    de Beer, M. M.
    van der Schaaf, J.
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2021, 163
  • [9] Limiting gas liquid flows and mass transfer in a novel rotating packed bed (HiGee)
    Rajan, Shashikant
    Kumar, Milan
    Ansari, M. Junaid
    Rao, D.P.
    Kaistha, Nitin
    Industrial and Engineering Chemistry Research, 2011, 50 (02): : 986 - 997
  • [10] Limiting Gas Liquid Flows and Mass Transfer in a Novel Rotating Packed Bed (HiGee)
    Rajan, Shashikant
    Kumar, Milan
    Ansari, M. Junaid
    Rao, D. P.
    Kaistha, Nitin
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (02) : 986 - 997