کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
201597 | 460559 | 2013 | 6 صفحه PDF | دانلود رایگان |
![عکس صفحه اول مقاله: Experiment and model for the surface tension of carbonated MEA–MDEA aqueous solutions Experiment and model for the surface tension of carbonated MEA–MDEA aqueous solutions](/preview/png/201597.png)
Surface tensions of CO2 unloaded and CO2 loaded MEA–MDEA aqueous solutions were measured by using the BZY-1 surface tension meter, which employs the Wilhemy plate principle. For CO2 unloaded solutions, the temperatures ranged from 293.15 to 333.15 K, and the mass fractions of MEA (wMEA) and MDEA (wMDEA) respectively ranged from 0.05 to 0.20, and 0.05 to 0.45. For CO2 loaded solutions, the temperatures ranged from 293.15 to 323.15 K, and wMEA and wMDEA respectively ranged from 0.05 to 0.10 and 0.30 to 0.45. The uncertainty of the surface tensions is ±0.1 mN m−1. A model was proposed to correlate the surface tensions of both CO2 loaded and CO2 unloaded solutions. For CO2 unloaded MEA–MDEA solutions, with 3 adjustable parameters as input, the average relative deviation (ARD) between experiments and calculations is 1.63%. For CO2 loaded MEA–MDEA solutions, with 5 adjustable parameters as input, ARD is 1.76%. The temperature, mass fractions of amines and CO2 loading dependence of the surface tensions were demonstrated on the basis of experiments and calculations.
► Surface tensions of carbonated MEA–MDEA aqueous solution were measured.
► Surface tensions of CO2 unloaded and loaded aqueous solutions were modeled.
► The decreasing surface tension is mainly due to increasing MDEA concentration.
► The effects of temperature, amine concentration and CO2 loading were demonstrated.
Journal: Fluid Phase Equilibria - Volume 337, 15 January 2013, Pages 83–88