https://doi.org/10.1016/j.cej.2022.138999 ” To further evaluate the predictive capability of the model, additional CO2 absorption experiments were carried out under different operating conditions and the corresponding results were
https://doi.org/10.1016/j.cej.2022.138999
https://doi.org/10.1016/j.cej.2022.138999 “The strategy adopted to simulate the experimental results relies on the classical homogeneous model for unstirred bubble column tank reactors operated continuously for the
https://doi.org/10.1016/j.egypro.2013.06.077
https://doi.org/10.1016/j.seppur.2021.118959 ” Advanced configurations that simplify the PFD with respect to the reference CAP configuration aim at reducing the investment costs associated with NH3-based capture
https://doi.org/10.1016/j.seppur.2021.118959 ” Power plants and most of the CO2 emitting industrial sectors, e.g. cement and steelwork plants, do not use strong acidic (or basic) solutions within their
https://doi.org/10.1016/j.seppur.2021.118959 ” Advanced process configurations have been assessed for inlet FG conditions corresponding to a typical European cement plant using the Best Available Technology (BAT),
https://doi.org/10.1016/j.egypro.2017.03.1270 ““
https://doi.org/10.1016/j.seppur.2021.118959 ” As mentioned above, the main contribution to the overall energy consumption of solvent-based CO2 capture processes is the thermal energy required in the CO2 desorber,
https://doi.org/10.1016/j.seppur.2021.118959 2.3.1. Technical Indicators Integrating the CO2 capture process by chemical absorption in a steam power plant has a significant impact on its overall performance, decreasing
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