17.06.2026

New publication online available!

CO2 loading estimates differences between 20 and 60 °C for an aqueous solvent with 0.5 M concentration in equilibrium with flue gas containing 0.15 mol/mol CO2.

In a new publication in Chemical Engineering and Processing: Process Intensification, Leandros Paschalidis and colleagues from TUHH show that CO2 desorption can occur well below the temperatures required for conventional steam stripping, opening pathways to low-temperature solvent regeneration.

Point-source carbon capture conventionally relies on steam stripping to regenerate chemical solvents. The approach is effective, since boiling the solvent simultaneously supplies heat and promotes CO2 desorption, but it creates a dependence on high-grade thermal energy and limits integration with low-temperature heat sources. The authors argue that its widespread use should not be interpreted as evidence that high-temperature regeneration is the only viable pathway for CO2 release.

Examining solvent regeneration through the lens of energy quality and temperature-sensitive thermodynamic control variables, they connect observations across buffer systems, sterically hindered and tertiary amines, thermomorphic solvents and enzymatically assisted capture to a common underlying mechanism: temperature dependent acid - base equilibria and phase behaviour that enable equilibrium driven desorption without vaporisation, with carbonic anhydrase emerging as a kinetic enabler under mild conditions. Viewed through this lens, the steam barrier is revealed as one of multiple design options rather than a physical inevitability, opening pathways toward carbon capture systems that are compatible with low-grade heat and offer improved exergy efficiency.

Leandros Paschalidis, Kai Fabian Kruber, Simon Müller, Mirko Skiborowski (2026). The steam barrier as a design constraint in carbon capture: Pathways to low-temperature regeneration. Chem. Eng. Process. 227, 110917.

https://doi.org/10.1016/j.cep.2026.110917