Kinematic viscosity of water at 22c7/2/2023 However, some new solvents are claimed to reduce the regeneration energy requirement. Proceedings of European Congress of Chemical Engineering (ECCE-6), 3, 57-61. First year operating experience with a 1 t/h CO2 absorption pilot plant at Esbjerg coal-fired power plant. , 2007 Knudsen, J., Vilhemsen, P.J., Jensen, J., Biede, O. Experience with CO2 capture from coal flue gas in pilot-scale: Testing of different amine solvents. Knudsen et al., 2009 Knudsen, J.N., Jensen, J.N., Vilhelmsen, P.J., Biede, O. Modelling and simulation of the Esbjerg pilot plant using the CESAR 1 solvent. Kvamsdal et al., 2011 Kvamsdal, H.M., Haugen, G., Svendsen, H.F., Tobiesen, A., Mangalapally, H., Hartono, A., Mejdell, T. Overall process analysis and optimisation for CO2 capture from coal fired power plants based on phase change solvents forming two liquid phases. The state of the art MEA is known to require 3.4-4 GJ/ton CO 2 ( Liebenthal et al., 2013 Liebenthal, U., Pinto, D.D.D., Monteiro, J.G.M.S., Svendsen, H.F., Kather, A. One of the major disadvantages of post-combustion capture processes is the process energy requirements. ) and monoethanolamine (MEA) is considered the benchmark solvent. International Journal of Greenhouse Gas Control, 68, 68-76 (2018). Influence of pKa on solvent performance of MAPA promoted tertiary amines. In the context of CO 2 removal from gas streams, absorption processes with alkanolamines are the state of the art ( Bernhardsen et al., 2018 Bernhardsen, I.M., Krokvik, I.R., Perinu, C., Pinto, D.D., Jens, K.J., Knuutila, H.K.
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