Development of process modelling

https://doi.org/10.1016/j.jece.2017.08.024 “Vapour-Liquid-Equilibrium (VLE) of the system CO2-MEA-H2O is of high importance to predict the desorption [35], [37]. Greer et al. [38] validated the simulation results from their Matlab model

https://doi.org/10.3390/en15020425 “The main cost metrics in this work were CO2 capture cost and CO2 avoided cost. Levelised cost or levelised cost of electricity (LCOE) for power plants’

https://doi.org/10.3390/en15020425 “The operating and maintenance costs in this work were divided into variable operating costs (VOCs) and fixed operating costs (FOCs). The economic assumptions utilised

https://doi.org/10.3390/en15020425 “The capital cost (CAPEX) in this work was estimated with the Enhanced Detailed Factor (EDF) method, which follows a bottom-up approach. The comprehensive details

https://doi.org/10.3390/en15020425 ” Initial cost estimation of heat exchangers is mainly based on the required heat exchange area. This is the surface area needed to effectively

https://doi.org/10.3390/en15020425 “The equipment sizing was based on the mass and energy balances from the process simulations. The approach was the same as that used in

https://doi.org/10.3390/en15020425 ” A 30 wt% monoethanolamine (MEA) process simulation for 90% CO2 capture from the two flue gases was performed in Aspen HYSYS Version 12. The

https://doi.org/10.3390/en15020425 “Two process configurations were also studied: the standard and the lean vapour compression (LVC) CO2 absorption and desorption models. The schematic descriptions of the two