(524c) Molecular Design of Optimum CO2 Capture Solvents: From Conceptual Screening to SAFT-Based Validation

Authors: 
Papadopoulos, A. I., Centre for Research and Technology-Hellas
Badr, S., Swiss Federal Institute of Technology, Zurich (ETHZ)
Chremos, A., Imperial College London
Forte, E., Imperial College London
Zarogiannis, T., Aristotle University of Thessaloniki
Seferlis, P., Aristotle University of Thessaloniki
Papadokonstantakis, S., Swiss Federal Institute of Technology, Zurich (ETHZ)
Adjiman, C. S., Imperial College London
Galindo, A., Imperial College London
Jackson, G., Imperial College London

The wide adoption of chemical absorption/desorption systems for post-combustion CO2 capture in industry is currently challenged by the high energy penalty in solvent regeneration and the environmental impacts associated with solvents and their derivatives. Intense research efforts reported in recent years are predominantly based on lab and pilot-scale experiments to select solvents which may potentially improve the overall performance of absorption/desorption CO2 capture. However, this is very challenging due to a) the highly non-ideal solvent-CO2-water chemical interactions, b) the countless combinations of potential capture solvent and blend candidates and c) the need for combined consideration of numerous thermodynamic, kinetic and sustainability properties as performance criteria prior to selecting solvents with optimum capture features. Computer-aided molecular design methods (CAMD) can help address these challenges and have been successful in supporting the synthesis of molecules with desired physical, chemical and environmental properties in non-CO2 separations [1]. Despite extensive developments in CAMD methods, few recent works have reported their utilization in the design of CO2 capture solvents or mixtures for chemical and physical absorption using the Statistical Associating Fluid Theory with potentials of Variable Range (SAFT-VR) [2, 3] and for physical absorption using the Perturbed Chain Polar Statistical Associating Fluid Theory (PCP-SAFT) [4]. While these approaches enable an accurate and reliable determination of solvent-process vapour-liquid equilibria, the set of few solvents screened to date will be further expanded as research efforts extend the rigorous predictive capabilities of SAFT-based models towards additional molecular structures. On the other hand, few CAMD approaches have also been reported [5, 6, 7] that use less accurate, but well-established group contribution methods to screen a much wider set of molecular structures by approximating as solvent performance criteria mainly properties relevant to thermodynamics and toxicity. 

In our current work, we propose the use of an optimization-based CAMD method to select post-combustion CO2 capture solvents of optimum performance in molecular and mixture properties associated with thermodynamics, kinetics and sustainability. The problem is first approached in a fast screening stage where solvent structures are evaluated based on the simultaneous consideration of important pure component properties. For the first time numerous properties are considered as performance criteria reflecting solvent characteristics based on thermodynamic (e.g., vapour pressure, CO2 solubility etc.), kinetic (solvent basicity, steric hindrance etc.) and sustainability (e.g., health and safety hazard, life cycle assessment etc.) behaviour. The simultaneous consideration of properties selected to capture the molecular chemistry effects on the absorption/desorption process compensates for the initial utilization of simpler models and ensures the selection of fewer but more effective solvents. A few highly-performing solvents are further evaluated using the SAFT-VR and SAFT-γ equations of state to predict accurately the very non-ideal solvent-water-CO2 mixture vapour-liquid equilibrium behaviour. Different functionalities of the employed CAMD method are used both to design optimum, novel molecular structures and to screen a dataset of commercially available amine solvents suitable for CO2 capture. The obtained results reveal interesting structure-property trade-offs and point to commercial molecules, which have very recently been considered or have yet to be employed as capture solvents.

Acknowledgements

Funding from the European Commission under grant FP7-ENERGY-2011-1-282789-CAPSOL is gratefully acknowledged.

Cited References

[1] Adjiman, C.S., Galindo, A., 2010, Process Systems Engineering: Volume 6: Molecular Systems Engineering, Pistikopoulos, E.N., Georgiadis, M.C., Dua, V. (Eds). 

[2] Mac Dowell N., Pereira F.E., Llovell F., Blas F.J., Adjiman C.S., Jackson G., Galindo A., 2011, Transferable SAFT-VR models for the calculation of the fluid phase equilibria in reactive mixtures of carbon dioxide, water, and n-alkylamines in the context of carbon capture, Journal of Physical Chemistry B, 115, 8155-8168.

[3] Pereira, F.E., Keskes, E., Galindo, A., Jackson, G., Adjiman, C.S., 2011, Integrated solvent and process design using a SAFT-VR thermodynamic description: High-pressure separation of carbon dioxide and methane, Computers and Chemical Engineering, 35 (3), 474-491.

[4] Bardow, A., Steur, K., Gross, J., 2010. Continuous-molecular targeting for integrated solvent and process design. Ind. Eng. Chem. Res. 49, 2834–2840.

[5] Juan Salazar, Urmila Diwekar, Kevin Joback, Adam H. Berger, Abhoyjit S. Bhown, Solvent Selection for Post-Combustion CO2 Capture, Energy Procedia, Volume 37, 2013, Pages 257-264

[6] Bommareddy, S., Chemmangattuvalappil, N.G., Solvason, C.C., Eden, M.R. Simultaneous solution of process and molecular design problems using an algebraic approach (2010) Computers and Chemical Engineering, 34 (9), pp. 1481-1486.

[7] Chemmangattuvalappil, N.G., Eden, M.R. A novel methodology for property-based molecular design using multiple topological indices (2013) Industrial and Engineering Chemistry Research, 52 (22), pp. 7090-7103.

Topics: