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  4. Continuous drying of alginate aerogel particles: Residence time measurement and process optimization under high pressure conditions
 
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Continuous drying of alginate aerogel particles: Residence time measurement and process optimization under high pressure conditions

Citation Link: https://doi.org/10.15480/882.16482
Publikationstyp
Journal Article
Date Issued
2026-05
Sprache
English
Author(s)
Manke, Erik  
Thermische Verfahrenstechnik V-8  
Rastar, Bennet  
Thermische Verfahrenstechnik V-8  
Bueno, Alberto  
Schroeter, Baldur  
Thermische Verfahrenstechnik V-8  
Smirnova, Irina  orcid-logo
Thermische Verfahrenstechnik V-8  
TORE-DOI
10.15480/882.16482
TORE-URI
https://hdl.handle.net/11420/60865
Journal
The journal of supercritical fluids  
Issue
231
Article Number
106888
Citation
The Journal of Supercritical Fluids 231: 106888 (2026)
Publisher DOI
10.1016/j.supflu.2026.106888
Scopus ID
2-s2.0-105027640820
Publisher
Elsevier
Peer Reviewed
true
This study advances continuous supercritical carbon dioxide (scCO₂) drying of aerogel particles by introducing a non-invasive optical method to determine particle residence time in a countercurrent extraction column. In countercurrent operation, scCO₂ flows upward while the particle suspension in ethanol enters from the top. The method enables precise, real-time residence time measurement under high pressure conditions without disturbing the process. The effects of pressure (100–150 bar), temperature (40–80 °C), CO₂ flow rate (30–80 g/min), and suspension flow rate (10–45 g/min) on residence time and drying efficiency were accordingly analyzed. Experiments were performed in a 1.25 m high extraction column, with an internal diameter of 20.5 mm, using highly spherical alginate beads with a diameter of ∼ 400 µm as a model system. Evidence of effective solvent removal throughout the whole operation range was provided by determination of the residual ethanol content in the intact aerogel beads after the drying process (0.0053–0.0341 gethanol/gaerogel). The dried products featured a specific surface area of 363 ± 27 m²/g, a mesopore volume of 3.2 ± 0.7 cm³ /g, consistent with the typical range of alginate aerogels. The combined insights provide a comprehensive picture of the countercurrent column’s operational response and allow the definition of practical operating windows. Elevated temperature and high pressure provide the most favorable trade-off between short residence time and minimized residual ethanol, maximizing the time-specific yield. Overall, the approach establishes a robust, transferable framework for optimizing continuous scCO₂ drying of aerogel particles and supports extension to other particle sizes and formulations.
Subjects
ScCO2 Aerogel drying
Continuous process
Optical RTD measurement
Countercurrent column
DDC Class
660: Chemistry; Chemical Engineering
Funding(s)
Projekt DEAL  
Lizenz
https://creativecommons.org/licenses/by/4.0/
Publication version
publishedVersion
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