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Minimising the regeneration heat duty of post-combustion CO2 capture by wet chemical absorption: The misguided focus on low heat of absorption solvents
Authors:Jochen Oexmann  Alfons Kather
Affiliation:1. School of Environmental Science and Engineering, North China Electric Power University, Baoding 071003, China;2. College of Environment, Zhejiang University of Technology, Hangzhou 310014, China;2. CSIRO Manufacturing, Clayton, Victoria 3168, Australia;3. CSIRO Energy, Newcastle, NSW 2300, Australia;1. Multi-phases Mass Transfer and Reaction Engineering Laboratory, College of Chemical Engineering, Sichuan University, Chengdu 610065, China;1. Department of Chemical Engineering, Indian Institute of Technology Kharagpur, Kharagpur 721302, India;2. Cryogenic Engineering Centre, Indian Institute of Technology Kharagpur, Kharagpur 721302, India;1. Process/Energy Systems Engineering Group, School of Engineering, University of Hull, HU6 7RX, UK;2. Telemark Technological Research and Development Centre (Tel-Tek), Norway
Abstract:An ideal solvent for CO2 capture by chemical absorption has to meet a number of requirements, such as high CO2 capacity, high rate of reaction, low costs, low corrosive behaviour, low degradation and low vapour pressure; above all, it has to show a low regeneration heat duty. This heat can be approximated as the sum of three terms: the sensible heat to raise the solvent from absorber to desorber temperature, the heat of evaporation required to produce the stripping steam in the reboiler, and the heat necessary to desorb the CO2 from the solution (heat of absorption).Many solvent screening studies focus almost exclusively on solvents that show a low heat of absorption. In these studies, the strong dependence of the three contributors to the overall regeneration heat duty on the chosen process parameters and on one another are often neglected.This work explains why the focus on solvents with a low heat of absorption, without considering the overall process, is not sufficient in quantifying the energy performance of alternative solvents. By using thermodynamic interrelations and underpinned by process simulations it is shown that operating parameters of the process, in particular the desorber pressure, must be taken into consideration in the evaluation of new solvents.
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