Kinetics of the absorption of carbon dioxide into aqueous hydroxides of lithium, sodium and potassium and blends of hydroxides and carbonates. (17th February 2015)

• Record Type: Journal Article
• Authors: Gondal, Shahla; Asif, Naveed; Svendsen, Hallvard F.; Knuutila, Hanna
• Is Part Of: Chemical engineering science. Volume 123(2015)
• Page Start: 487
• Page End: 499
• Publication Date: 2015-02-17
• Subjects: Chemical engineering -- Periodicals; Génie chimique -- Périodiques; Chemical engineering; Periodicals; Electronic journals; 660
• DOI: 10.1016/j.ces.2014.10.038
• Languages: English
• ISSNs: 0009-2509

Abstract

Abstract: In the present work the rates of absorption of carbon dioxide into aqueous hydroxides (0.01–2.0 kmol.m −3 ) and blends of hydroxides and carbonates with mixed counter ions (1–3 kmol.m −3 ) containing Li +, Na + and K + as cations were studied in a String of Discs Contactor (SDC). The temperature range was 25–64 °C and the conditions were such that the reaction of CO2 could be assumed pseudo-first-order. The dependence of the reaction rate constant on temperature and concentration/ionic strength and the effect of counter ions were verified for the reaction of CO2 with hydroxyl ions in these aqueous electrolyte solutions. The infinite dilution second order rate constant k O H − ∞ was derived as an Arrhenius temperature function and the ionic strength dependency of the second order rate constant, k O H −, was validated by the widely used Pohorecki and Moniuk model (Pohorecki and Moniuk, 1988 ) with refitted parameters. The contribution of ions to the ionic strength and the model itself, was extended to the given concentration and temperature ranges. The model with refitted parameters represents the experimental data with less than 12% AARD. Highlights: CO2 absorption kinetics of hydroxides and carbonates of Li +, Na + and K + are studied in SDC. The measured data range from 0.01–3 M hydroxides and carbonates at 25–64 °C. The measured kinetic data are used to derive infinite dilution second order rate constant. The derived infinite dilution second order rate constant is compared with literature. New modeling parameters for second order rate constant are proposed.