Towards the digital extraction column: Online-monitoring and analysis of fluid dynamics in liquid-liquid extraction columns

被引:0
作者
Palmtag, Andreas [1 ]
Lehmann, Lorenz [1 ]
Hanz, Leon Rojas [1 ]
Kiseleva, Uliana [1 ]
Jupke, Andreas [1 ]
机构
[1] Rhein Westfal TH Aachen, Fluid Proc Engn AVT FVT, Forckenbeckstr 51, D-52074 Aachen, Germany
来源
CHEMICAL ENGINEERING JOURNAL ADVANCES | 2025年 / 22卷
关键词
Multi-object tracking; Process monitoring; Liquid-liquid extraction; Pulsed sieve tray extraction columns; Yolov8; Bytetrack; Drop sedimentation; POPULATION BALANCES; PREDICTION; VELOCITIES; SYSTEMS; SIZE;
D O I
10.1016/j.ceja.2025.100727
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
An effective monitoring system for liquid-liquid extraction columns must evaluate key fluid dynamic properties such as Sauter mean diameter, the hold-up of the dispersed phase, and the drop sedimentation velocity to accurately estimate the available mass transfer area and the solvent residence time. However, while many studies have focused on investigating the hold-up and the drop size distribution (DSD) studies on drop sedimentation remain scarce, often leading to its estimation based on the remaining fluid dynamic properties. In this work, we introduce a column monitoring system that enables a holistic assessment of the column operation based on all three fluid dynamic properties. For this purpose, we used the differential pressure method to determine the holdup, and two telecentric camera setups to determine the Sauter mean diameter, and the drop sedimentation velocity. The camera images were processed by YOLOv8 for drop detection and the ByteTrack algorithm for drop tracking, achieving high accuracy on unseen data. In an extensive experimental study, we investigated the interdependency of the fluid dynamic properties at different operating conditions including flooding in a DN50 pulsed sieve tray extraction column. The obtained experimental data was used to parametrize a drop sedimentation model. Our findings indicate that assuming a constant swarm exponent in the model is inadequate, particularly at lower liquid loads.
引用
收藏
页数:17
相关论文
共 52 条
  • [1] BAILES PJ, 1986, CHEM ENG RES DES, V64, P43
  • [2] Population Balances for Extraction Column Simulations-An Overview
    Bart, Hans-Joerg
    Jildeh, Hanin
    Attarakih, Menwer
    [J]. SOLVENT EXTRACTION AND ION EXCHANGE, 2020, 38 (01) : 14 - 65
  • [3] Bergstra J., 2013, INT C MACHINE LEARNI, P115, DOI [DOI 10.5555/3042817.3042832, 10.5555/3042817.3042832]
  • [4] BUBBLE SIZE AND BUBBLE VELOCITY DISTRIBUTION IN BUBBLE COLUMNS UNDER INDUSTRIAL CONDITIONS
    Bothe, Melanie
    Christlieb, Marc-Andreas
    Hoffmann, Marko
    Tedjasukmana, Osmond
    Michaux, Frank
    Rollbusch, Philipp
    Becker, Marc
    Schueteer, Michael
    [J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2017, 95 (05) : 902 - 912
  • [5] Mini-batch settling cell for investigation of liquid-liquid phase separation
    Eberz, Joerg
    Sibirtsev, Stepan
    Jupke, Andreas
    [J]. CHEMICAL ENGINEERING SCIENCE, 2025, 301
  • [6] Fleet D., 2014, Computer Vision-ECCV 2014
  • [7] Decoupled IoU Regression for Object Detection
    Gao, Yan
    Wang, Qimeng
    Tang, Xu
    Wang, Haochen
    Ding, Fei
    Li, Jing
    Hu, Yao
    [J]. PROCEEDINGS OF THE 29TH ACM INTERNATIONAL CONFERENCE ON MULTIMEDIA, MM 2021, 2021, : 5628 - 5636
  • [8] Godfrey J.C., 1990, Chem. Eng. Res. Des., P130
  • [9] Goedecke Ralf., 2006, FLUIDVERFAHRENSTECHN
  • [10] Bubble up: Tracking down the vertical velocity of oxygen bubbles in parallel plate electrolyzers using CNN
    Goertz, Jonas
    Seiler, Jakob
    Jupke, Andreas
    [J]. INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2024, 177