Equilibrium loadings and adsorption isotherm model parameters estimated from multi-component breakthrough curves

被引:0
|
作者
Zarei, Somayeh [1 ]
Harriehausen, Isabel [1 ]
Lee, Ju Weon [1 ]
Seidel-Morgenstern, Andreas [1 ]
机构
[1] Max Planck Inst Dynam Complex Tech Syst, Sandtor str 1, D-39106 Magdeburg, Germany
关键词
Adsorption isotherm determination; Equilibrium theory; Langmuir isotherm model; Breakthrough curves; Ternary systems;
D O I
10.1007/s10450-024-00549-5
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Quantitative knowledge of competitive adsorption isotherms is essential for the design and optimization of adsorption based separation processes. Since the experimental determination of these thermodynamic functions is complicated and time consuming, there is a need for fast and easy to apply methods. In particular attractive are methods that evaluate measured breakthrough curves (BTC). Key features of these curves can be predicted with the equilibrium theory, which ignores kinetic effects that cause band broadening. If the adsorption equilibria can be described by the classical competitive Langmuir isotherm model, outlet concentration profiles can be calculated analytically. The paper summarizes and illustrates well-known classical results for N-component systems. The theory is applied to analyze experimentally determined BTC for a ternary mixture fed into an initially fully regenerated column under constant flowrate and under isothermal conditions. It is demonstrated that the retention times and intermediate plateau concentrations, which are observable for example in a single ternary BTC experiment, allow estimating a defined number of characteristic equilibrium loadings. These loadings can be directly used for easy estimation of the parameters of an assumed isotherm model. Various possibilities to use a reduced number of loadings and to include complementary results of standard pulse experiments are described. The isotherms generated from the ternary BTC are successfully validated by results of single component and ternary BTC experiments carried out subsequently. Options to generalize the method to determine isotherm model parameters from measured BTC to initially preloaded columns and to more complex mixtures are finally outlined. An equilibrium theory based dynamic method for determining adsorption isotherms from measured breakthrough curves is described.The method exploits understanding of the column dynamics offered by classical equilibrium theory.It allows estimating characteristic mixture and single component loadings, which can be used to estimate the parameters of an isotherm model.The method is validated analyzing BTC recorded for a ternary system, which follows the competitive Langmuir isotherm model.It is attractive for quickly estimating adsorption capacities and isotherm courses.
引用
收藏
页码:2295 / 2312
页数:18
相关论文
共 50 条
  • [1] Predicting of breakthrough curves for single- and multi-component adsorption of pollutants on actived carbon filters
    Neitsch, Marcel
    Suckow, Matthias
    Heschel, Wolfgang
    Chemische Technik (Leipzig), 1999, 51 (02): : 55 - 63
  • [2] Simultaneous determination of multi-component isotherm parameters from single sample of liquid
    Satoh, K
    Chang, HT
    Hattori, H
    Tajima, K
    Furuya, E
    ADSORPTION-JOURNAL OF THE INTERNATIONAL ADSORPTION SOCIETY, 2005, 11 (Suppl 1): : 79 - 83
  • [3] Simultaneous Determination of Multi-Component Isotherm Parameters from Single Sample of Liquid
    Kohei Satoh
    H. Ted Chang
    Hideo Hattori
    Kiyohiko Tajima
    Eiji Furuya
    Adsorption, 2005, 11 : 79 - 83
  • [4] Mathematical Modeling of Single and Multi-Component Adsorption Fixed Beds to Rigorously Predict the Mass Transfer Zone and Breakthrough Curves
    Siahpoosh, Mohsen
    Fatemi, Shohreh
    Vatani, Ali
    IRANIAN JOURNAL OF CHEMISTRY & CHEMICAL ENGINEERING-INTERNATIONAL ENGLISH EDITION, 2009, 28 (03): : 25 - 44
  • [5] ESTIMATION OF COMPONENT LOADINGS IN FIXED-BED ADSORPTION FROM BREAKTHROUGH CURVES OF BINARY GAS-MIXTURES IN NONTRACE SYSTEMS
    KLUGE, G
    FRANKE, T
    SCHOLLNER, R
    CHEMICAL ENGINEERING SCIENCE, 1991, 46 (01) : 368 - 371
  • [6] Equilibrium adsorption data from breakthrough curves with variable velocity and pressure
    Foeth, F
    Bosch, H
    Sjostrand, A
    Aly, G
    Reith, T
    SEPARATION SCIENCE AND TECHNOLOGY, 1996, 31 (01) : 21 - 38
  • [8] Adsorption model for multi-component heavy metal ions on clay based on non-equilibrium thermodynamics
    Zhang Z.-H.
    Zhang J.-P.
    Yantu Gongcheng Xuebao/Chinese Journal of Geotechnical Engineering, 2019, 41 (05): : 829 - 835
  • [9] Direct calculation of the equilibrium composition for multi-component Langmuir isotherms in batch adsorption
    Kaiblinger, Norbert
    Hahn, Rainer
    Beck, Jurgen
    Wang, Yiran
    Carta, Giorgio
    ADSORPTION-JOURNAL OF THE INTERNATIONAL ADSORPTION SOCIETY, 2024, 30 (01): : 51 - 56
  • [10] Direct calculation of the equilibrium composition for multi-component Langmuir isotherms in batch adsorption
    Norbert Kaiblinger
    Rainer Hahn
    Jürgen Beck
    Yiran Wang
    Giorgio Carta
    Adsorption, 2024, 30 : 51 - 56