Your browser doesn't support javascript.
loading
Effect of Blending Ratio and Temperature on CO2 Solubility in Blended Aqueous Solution of Monoethanolamine and 2-Amino-2-methyl-propanol: Experimental and Modeling Study Using the Electrolyte Nonrandom Two-Liquid Model.
Choi, Bong-Keun; Kim, Seung-Mo; Lee, Jong-Seop; Park, Young Cheol; Chun, Dong-Hyuk; Shin, Hun-Yong; Sung, Hyun-Je; Min, Byoung-Moo; Moon, Jong-Ho.
Afiliação
  • Choi BK; Department of Chemical Engineering, Chungbuk National University, Cheongju, Chungbuk 28644, Korea.
  • Kim SM; Department of Chemical Engineering, Chungbuk National University, Cheongju, Chungbuk 28644, Korea.
  • Lee JS; Korea Institute of Energy Research, 102 Gajeong-ro, Yuseong-gu, Daejeon 34129, Korea.
  • Park YC; Korea Institute of Energy Research, 102 Gajeong-ro, Yuseong-gu, Daejeon 34129, Korea.
  • Chun DH; Korea Institute of Energy Research, 102 Gajeong-ro, Yuseong-gu, Daejeon 34129, Korea.
  • Shin HY; Seoul National University of Science & Technology, 232 Gongneung-ro, Nowon-gu, Seoul 01811, Korea.
  • Sung HJ; Research Laboratory, Hansol EME, Seongnam 13591, Korea.
  • Min BM; Korea Institute of Energy Research, 102 Gajeong-ro, Yuseong-gu, Daejeon 34129, Korea.
  • Moon JH; Department of Chemical Engineering, Chungbuk National University, Cheongju, Chungbuk 28644, Korea.
ACS Omega ; 5(44): 28738-28748, 2020 Nov 10.
Article em En | MEDLINE | ID: mdl-33195927
ABSTRACT
This paper reports the newly measured experimental data for CO2 solubility in a blended aqueous solution of monoethanolamine (MEA) and 2-amino-2-methyl-propanol (AMP) at different amine mixing ratios (MEA/AMP/H2O = 92170, 151570, and 21970 wt %) and working temperatures (323.15, 373.15, and 383.15 K). The successive substitution method was used for calculating the mole fractions of all molecules (four molecules) and electrolytes (three cations and four anions) from the equilibrium along with the material and charge balance equations (11 equations). The electrolyte nonrandom two-liquid (e-NRTL) model was used to investigate nonideality in the liquid phase. Using the abovementioned thermodynamic models, the partial pressures of CO2 in the gas phase, mole fractions of all components in the liquid phase, pH variations, heats of absorption, and cyclic capacities of CO2 according to the absorption/desorption temperature and the blending ratio of MEA/AMP were estimated.

Texto completo: 1 Coleções: 01-internacional Base de dados: MEDLINE Idioma: En Ano de publicação: 2020 Tipo de documento: Article

Texto completo: 1 Coleções: 01-internacional Base de dados: MEDLINE Idioma: En Ano de publicação: 2020 Tipo de documento: Article