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 ” Fig. 3(a) shows the optimization results considering only the performance of the FG-WW column and of the NH3 desorber, in the plane ωFG−WW–PrFG−WW: Greater NH3 concentration in
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/10.2516/ogst/2013160 “Ammonia is very volatile and characterised by high equilibrium pressure even in the CO2 loaded aqueous ammonia solution. Figure 9 shows predicted partial and
A free platform to share knowledge of science and engineering. Extensive analysis of literature and summarized review in carbon capture science and technology.
© 2022 Science-Share.com.All Rights Reserved.