A mechanistic process model for aqueous two-phase flotation: Insights into enzyme transport mechanisms
Continuous aqueous two-phase flotation (ATPF) is an alternative downstream approach for the selective separation of enzymes from complex biosuspensions. Until now, mass transport across the phase interface has been assumed to be mainly due to accumulation of enzymes on the surface of rising gas bubbles (flotation), while theoretical studies are lacking. This work presents a mechanistic compartment model of the ATPF process that that also includes mass transport by extraction, i.e. diffusion across the phase interface. The model is validated with ATPF experiments over a wide range of process parameters and reliably predicts the process behavior. The results indicate that extraction accounts for more than 80% of the integral mass transfer, while bubbles are still essential for phase mixing and the creation of a large interfacial area. Therefore, the proposed process model provides valuable insights into the enzyme transport mechanisms and enables future developments such as model predictive control. • A mechanistic process model for continuous aqueous two-phase flota- tion (ATPF) is proposed. • The model is capable of accurately describing experimental data with wide variations in process parameters. • Extraction is identified as the main mass transport mechanism across the phase interface.
Authors
- Frank Rhein (ORCID: https://orcid.org/0000-0002-7654-3824)
- Hermann Nirschl (ORCID: https://orcid.org/0000-0001-6398-1692)
- Kim Carina Lohfink (ORCID: https://orcid.org/0009-0009-1321-7720)
Institutions
- Karlsruhe Institute of Technology (DE)
Publication Details
- Journal
- Separation and Purification Technology
- Published
- 2025-05-03
- DOI
- https://doi.org/10.1016/j.seppur.2025.133100
- Primary Topic
- Minerals Flotation and Separation Techniques
- Type
- article
- Field-Weighted Citation Impact
- 0.00
Funders
- Deutsche Forschungsgemeinschaft