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  4. Reconstruction-free EIT for injection-pattern classification and superficial gas velocity regression as proxies for local gas holdup in bubble columns

Reconstruction-free EIT for injection-pattern classification and superficial gas velocity regression as proxies for local gas holdup in bubble columns

Citation Link: https://doi.org/10.15480/882.18619
Publikationstyp
Journal Article
Date Issued
2026-09-10
Sprache
English
Author(s)
Hollenberg, Moritz
Mechatronik im Maschinenbau M-4
Ostovar, Hossein
Chemische Reaktionstechnik V-2
Sharafian, Zahra
Chemische Reaktionstechnik V-2
Liebing, Tom
Mechatronik im Maschinenbau M-4
Korup, Oliver
Chemische Reaktionstechnik V-2
Kern, Thorsten Alexander
Mechatronik im Maschinenbau M-4
Horn, Raimund
Chemische Reaktionstechnik V-2
TORE-DOI
10.15480/882.18619
TORE-URI
https://hdl.handle.net/11420/65052
Journal
Industrial & engineering chemistry research
Volume
65
Issue
37
Start Page
19801
End Page
19817
Citation
Industrial & Engineering Chemistry Research 65 (37): 19801–19817 (2026)
Publisher DOI
10.1021/acs.iecr.6c01116
Scopus ID
2-s2.0-105051568218
Publisher
American Chemical Society (ACS)
Is Supplemented By
https://zenodo.org/records/21773393
https://zenodo.org/records/21167281
Electrical impedance tomography (EIT) as a noninvasive tomographic technique is increasingly applied to multiphase reactor monitoring; however, conventional image reconstruction is ill-posed and regularization-dependent and may be redundant in applications where the primary objective is operating-state identification rather than explicit spatial conductivity field reconstruction. Here, we present a reconstruction-free, measurement-domain framework for bubble-column monitoring that maps raw complex boundary impedance data directly to two reactor-relevant inference tasks: (i) gas injection pattern classification and (ii) superficial gas velocities regression. Together, these two quantities ─ the spatial injection distribution and the total volumetric flow ─ constitute the primary process-state information from which gas holdup can subsequently be inferred and are therefore reported as proxies for local gas holdup monitoring. Experiments were conducted in an acrylic bubble column (600 mm height, 104 mm inner diameter) equipped with a 256-electrode array distributed over eight axial rings and operated at four excitation frequencies (1 kHz-1 MHz). Experiments covered gas flow rates between 1.0 and 6.5 L min–1 (Ug = 1.96 → 12.75 mm s–1), within which near-perfect gas injection pattern classification was achieved with accuracies of 93–100% for excitation frequencies between 1 and 100 kHz using the full 256-electrode configuration. For quantitative superficial gas velocity estimation, increasing calibration density along Ug reduced the mean absolute error from 0.388 to 0.105 L min–1 (MAE[Ug] = 0.76 → 0.205 mm s–1, i.e. 7.0% → 1.9% of the operating range) for localized injection and from 0.298 to 0.157 L min–1 (MAE[Ug] = 0.585 → 0.307 mm s–1, i.e. 5.4% → 2.8% of the operating range) for distributed injection conditions. These results demonstrate that direct inference from raw EIT boundary measurements enables accurate, real-time monitoring of bubble-column operation without tomographic reconstruction and provide quantitative guidance on excitation frequency selection, axial sensing placement, and calibration resolution.
DDC Class
620.1: Engineering Mechanics and Materials Science
Funding(s)
SFB 1615 - SMARTe Reaktoren für die Verfahrenstechnik der Zukunft
SFB 1615 - Teilprojekt A02: Quantitative elektrische 3D-Impedanztomographie in Echtzeit für Mehrphasenreaktoren
United Nations University Hub on Engineering to Face Climate Change at Hamburg University of Technology
Lizenz
https://creativecommons.org/licenses/by/4.0/
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