Entransy dissipation analysis of interfacial convection enhancing gas-liquid mass transfer process based on field synergy principle

被引:7
|
作者
Li, Dong [1 ]
Zeng, Aiwu [1 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, State Key Lab Chem Engn, Tianjin 300350, Peoples R China
关键词
Field synergy; Mass entransy dissipation; Equivalent mass resistance; Interfacial convection; Reinforcement; HEAT-TRANSFER; RAYLEIGH CONVECTION; NATURAL-CONVECTION; CARBON-DIOXIDE; OPTIMIZATION; DIFFUSION; ABSORPTION; SIMULATION; BUOYANCY; SURFACES;
D O I
10.1016/j.cjche.2019.03.017
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
An exploration of the gas CO2 absorbed into liquid ethanol accompanied with Rayleigh convection is performed by analyzing the mass entransy dissipation; this new statistical quantity is introduced to describe the irreversibility of mass transfer potential capacity. Based on the general advection-diffusion differential equation for an unsteady mass transfer process, the variation of the included angle between the velocity vector and concentration gradient fields is investigated to reveal the underlying mechanism of interfacial convection enhancing mass transfer. Results show some identical characteristics with the qualitative analyses of the synergy effects generated by the concentration and velocity fields after interfacial convection occurring for a boundary condition of fixed surface concentration. And the equivalent mass resistance for convective mass transfer process presents the similar variation with the reciprocal of instantaneous mass transfer coefficient. Accordingly, it is reasonable to be seen that mass transfer dissipation rate could be provided to assess the convection strength and explain fundamentally how Rayleigh convection improves mass transfer performance through establishing a close relationship between the mass transfer capacity and field synergy principle from the view of mass transfer theory. (C) 2019 The Chemical Industry and Engineering Society of China, and Chemical Industry Press Co., Ltd. All rights reserved.
引用
收藏
页码:1777 / 1788
页数:12
相关论文
共 45 条
  • [21] Turbulent Convection Heat Transfer Analysis of Supercritical Pressure CO2 Flow in a Vertical Tube Based on the Field Synergy Principle
    Wang, Zhen-Chuan
    Jiang, Pei-Xue
    Xu, Rui-Na
    HEAT TRANSFER ENGINEERING, 2019, 40 (5-6) : 476 - 486
  • [22] Numerical analysis of heat transfer in unglazed transpired collectors based on field synergy principle
    Gao, Lixin
    Bai, Hua
    Wu, Xing
    SOLAR ENERGY, 2013, 95 : 336 - 344
  • [23] Numerical Analysis of Liquid Potassium Flow and Heat Transfer in a Core for Space Nuclear Reactor Based on Entransy Dissipation Theory
    Sun, Qi-Qi
    Zhang, Hao-Chun
    Sun, Zi-Jian
    JOURNAL OF THERMAL SCIENCE AND ENGINEERING APPLICATIONS, 2023, 15 (06)
  • [24] Advanced analysis of liquid dispersion and gas-liquid mass transfer in a bubble column with dense vertical internals
    Moeller, Felix
    MacIsaac, Alan
    Lau, Yuk Man
    Schleicher, Eckhard
    Hampel, Uwe
    Schubert, Markus
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 2018, 134 : 575 - 588
  • [25] Ultrasound-assisted gas-liquid mass transfer process in microreactors: The influence of surfactant, channel size and ultrasound frequency
    Zhang, Qiang
    Dong, Zhengya
    Zhao, Shuainan
    Liu, Zhikai
    Chen, Guangwen
    CHEMICAL ENGINEERING JOURNAL, 2021, 405 (405)
  • [26] Flow and heat transfer analysis in porous wick of CPL evaporator based on field synergy principle
    Z. C. Liu
    W. Liu
    A. Nakayama
    Heat and Mass Transfer, 2007, 43 : 1273 - 1281
  • [27] Hydrodynamic and mass transfer parameters in agitated reactors part II: Gas-holdup, sauter mean bubble diameters, volumetric mass transfer coefficients, gas-liquid interfacial areas, and liquid-side mass transfer coefficients
    Lemoine, R
    Morsi, B
    INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2005, 3
  • [28] INTERFACIAL AREA AND MASS-TRANSFER IN GAS-LIQUID COCURRENT UPFLOW AND COUNTERCURRENT-FLOW IN RECIPROCATING PLATE COLUMN
    SUNDARESAN, A
    VARMA, YBG
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1990, 68 (06) : 952 - 958
  • [29] Gas-liquid mass transfer in co-current three-phase fluidized beds with non-Newtonian fluids: Theoretical models based on the energy dissipation rate
    Miura, Hideki
    Katoh, Takashi
    Kawase, Yoshinori
    CHEMICAL ENGINEERING JOURNAL, 2012, 185 : 337 - 346
  • [30] EXPERIMENTAL STUDY OF GAS-LIQUID MASS TRANSFER IN A RECTANGULAR MICROCHANNEL BY DIGITAL IMAGE ANALYSIS METHOD
    Yang, Shuo
    Kong, Gaopan
    Wu, Zan
    PROCEEDINGS OF ASME 2021 INTERNATIONAL MECHANICAL ENGINEERING CONGRESS AND EXPOSITION (IMECE2021), VOL 10, 2021,