Abstract
In this work, a physicochemical absorbent was proposed for CO2 capture, which consists of dibutyl ether as physical solvent, N-methylethanolamine (NMEA) as chemical additive, and ethanol as dissolvent. The vapor–liquid equilibrium behavior of this CO2 + physicochemical absorbent system was measured using an isothermal synthetic apparatus. The solubility data of CO2 in ethanol at 313.15 K were measured and compared with literature data to verify the validity of this method. Then, the CO2 solubility data of above system with varying NMEA mass fractions of 15 %, 25 %, and 50 % were, respectively, measured at 298.15 K. It shows that the CO2 solubility increases when NMEA mass fraction goes up. The CO2 solubility data in the absorbent with 25 % NMEA mass fraction were measured at a temperature range from 298.15 K to 328.15 K with the interval of 10 K and at a pressure range from 0 MPa to 3 MPa. The result shows that CO2 turns out to be more soluble in the physicochemical absorbents than in dibutyl ether at the same conditions of temperature and pressure.
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Abbreviations
- a :
-
CO2 solubility (mol·kg−1)
- ARD :
-
Absolute relative deviation
- M :
-
Molecular weight (g·mol−1)
- m :
-
Mass (g)
- n :
-
Number of moles (mol)
- T :
-
Temperature (K)
- p :
-
Pressure (Pa)
- R 2 :
-
Correlation coefficient
- w :
-
Mass fraction
- ω :
-
Acentric factor
- δ :
-
Increase rate
- c:
-
Critical values
- corr:
-
Correlated values
- DBE:
-
Dibutyl ether
- EL:
-
Ethanol
- exp:
-
Experimental values
- lit:
-
Literature values
- NMEA:
-
N-methylethanolamine
- TEA:
-
Triethanolamine
- MDEA:
-
Methyldiethanolamine
- PR:
-
Peng–Robinson
- SRK:
-
Soave–Redlich–Kwong
- pc:
-
Physicochemical solvent
- solv:
-
Solvent
References
S. Ma’mun, Selection and Characterization of New Absorbents for Carbon Dioxide Capture, Norwegian University of Science and Technology, Faculty of Natural Sciences and Technology, Department of Chemical Engineering, 2005
IPCC (Intergovernmental Pannel on Climate Change - IPCC), Climate Change 2007 (2007)
W. Huang, Y. Mi, Y. Li, D. Zheng, Ind. Eng. Chem. Res. 54, 3430 (2015)
M. Zhang, Y. Guo, Appl. Energy 111, 142 (2013)
W. Zhao, G. Sprachmann, Z. Li, N. Cai, X. Zhang, Appl. Energy 112, 381 (2013)
T. Wang, C. Hou, K. Ge, K.S. Lackner, X. Shi, J. Liu, M. Fang, Z. Luo, J. Phys. Chem. Lett. 3986 (2017)
P.D. Vaidya, V.V. Mahajani, Ind. Eng. Chem. Res. 44, 1868 (2005)
R. Pohorecki, C. Możeński, Chem. Eng. Process. Process Intensif. 37, 69 (1998)
A. Henni, A.E. Mather, J. Chem. Eng. Data 40, 493 (1995)
F. Murrieta-Guevara, E. Rebolledo-Libreros, A. Trejo, J. Chem. Eng. Data 37, 4 (1992)
S.-B. Park, H. Lee, K.-H. Lee, Int. J. Thermophys. 19, 1421 (1998)
X. Wu, X. Du, D. Zheng, Int. J. Thermophys. 31, 308 (2010)
J. Na, B.-M. Min, J.-H. Moon, J.-S. Lee, H.Y. Shin, Int. J. Thermophys. 39, 96 (2018)
K. Fischer, M. Wilken, J. Chem. Thermodyn. 33, 1285 (2001)
K. Fischer, J. Gmehling, J. Chem. Eng. Data 39, 309 (1994)
W. Huang, G. Sun, D. Zheng, L. Dong, X. Wu, J. Chen, J. Chem. Eng. Data 58, 1354 (2013)
J. Klimeck, R. Kleinrahm, W. Wagner, J. Chem. Thermodyn. 33, 251 (2001)
J.H. Dymond, K.N. Marsh, R.C. Wilhoit, K.C. Wong, Virial Coefficients of Pure Gases and Mixtures (2002)
D.Y. Peng, D.B. Robinson, Ind. Eng. Chem. Fundam. (1976)
G. Soave, Chem. Eng. Sci. (1972)
R. Sidi-Boumedine, S. Horstmann, K. Fischer, E. Provost, W. Fürst, J. Gmehling, Fluid Phase Equilib. 218, 85 (2004)
D. Silkenbäumer, B. Rumpf, R.N. Lichtenthaler, Ind. Eng. Chem. Res. 37, 3133 (1998)
K.E. Starling, AIChE J. 24, 1142 (2018)
Y. Li, X. Chen, W. Huang, J. Yang, J. Chem. Thermodyn. 122, 133 (2018)
Y. Li, W. Huang, D. Zheng, Y. Mi, L. Dong, Fluid Phase Equilib. 370, 1 (2014)
Y. Li, Q. Liu, W. Huang, J. Yang, J. Chem. Thermodyn. 127, 25 (2018)
Y. Li, Q. Liu, W. Huang, J. Yang, J. Chem. Thermodyn. 127, 71 (2018)
K. Suzuki, H. Sue, M. Itou, R.L. Smith, H. Inomata, K. Arai, S. Saito, J. Chem. Eng. Data 35, 63 (1990)
I. Tsivintzelis, D. Missopolinou, K. Kalogiannis, C. Panayiotou, Fluid Phase Equilib. 224, 89 (2004)
X. Du, Measurement and Modeling of CO 2 Solubility in Butyl Ether and a Complex Absorbent, Beijing University of Chemical Technology, 2010
Acknowledgments
This research was supported by the National Natural Science Foundation of China (Nos. 51741605, 51706146, and 21506124), and Capacity Building Plan for some Non-military Universities and Colleges of Shanghai Scientific Committee (No. 18060502600). This research was also sponsored by Shanghai Sailing Program (No. 19YF1434800).
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Huang, W., Du, X., Zheng, D. et al. CO2 Solubility in Physicochemical Absorbent: Dibutyl Ether/N-Methylethanolamine/Ethanol. Int J Thermophys 40, 43 (2019). https://doi.org/10.1007/s10765-019-2506-4
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DOI: https://doi.org/10.1007/s10765-019-2506-4