Transient modeling of extraction columns: Parameter estimation, uncertainty analysis, and operation optimization

Abstract Despite extensive modeling efforts in extraction research, transient column models are rarely applied in industry due to concerns regarding parameter identifiability and model reliability. To address this, we analyzed uncertainty propagation from estimated parameters in a previously introduced column model and assessed identifiability via ill‐conditioning analysis. Extrapolation was evaluated by estimating parameters from fluid dynamic experiments and validating with mass transfer data. Using a DN50 pulsed sieve tray column, parameters , and the swarm exponent were estimated through maximum likelihood, as they directly affect online‐measurable drop diameter and hold‐up . Incorporating these estimates, the model reproduced , , and stationary and transient concentration profiles with relative errors below 10%. For optimization, we applied the model to minimize solvent demand for 99% product recovery. Uncertainty analysis showed coefficients of variation below 4%, confirming model reliability.

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Publication Details

Journal
AIChE Journal
Published
2026-02-05
DOI
https://doi.org/10.1002/aic.70227
Primary Topic
Process Optimization and Integration
Type
article
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article

Transient modeling of extraction columns: Parameter estimation, uncertainty analysis, and operation optimization

Andreas Palmtag, Andreas Jupke, Jannik Dohmen
AIChE Journal
Process Optimization and Integration
article

Transient modeling of extraction columns: Parameter estimation, uncertainty analysis, and operation optimization

Andreas Palmtag, Andreas Jupke, Jannik Dohmen
article en

Abstract

Abstract Despite extensive modeling efforts in extraction research, transient column models are rarely applied in industry due to concerns regarding parameter identifiability and model reliability. To address this, we analyzed uncertainty propagation from estimated parameters in a previously introduced column model and assessed identifiability via ill‐conditioning analysis. Extrapolation was evaluated by estimating parameters from fluid dynamic experiments and validating with mass transfer data. Using a DN50 pulsed sieve tray column, parameters , and the swarm exponent were estimated through maximum likelihood, as they directly affect online‐measurable drop diameter and hold‐up . Incorporating these estimates, the model reproduced , , and stationary and transient concentration profiles with relative errors below 10%. For optimization, we applied the model to minimize solvent demand for 99% product recovery. Uncertainty analysis showed coefficients of variation below 4%, confirming model reliability.

AIChE Journal
Forschungszentrum Jülich (DE), RWTH Aachen University (DE)
Industry, innovation and infrastructure
Openalex Percentile: Top 66%
Process Optimization and Integration
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