216
L. F. Vega et al.
98. Llovell F, Pàmies JC, Vega LF (2004) Thermodynamic properties of Lennard-Jones chain
molecules: renormalization-group corrections to a modified statistical associating fluid theory.
J Chem Phys 121(21):10715–10724
99. Lemmon E, Huber M, McLinden M (2013) NIST standard reference database 23: reference
fluid thermodynamic and transport properties-REFPROP, version 9.1. Standard reference data
program. National Institute of Standards and Technology, Gaithersburg
100. Pádua AAH, Fareleira JMNA, Calado JCG, Wakeham WA (1996) Density and viscosity
measurements of 1,1,1,2-tetrafluoroethane (HFC-134a) from 199 K to 298 K and up to 100
MPa. J Chem Eng Data 41(4):731–735
101. Oliveira CMBP, Wakeham WA (1993) The viscosity of liquid R134a. Int J Thermophys
14(1):33–44
102. Diller DE, Peterson SM (1993) Measurements of the viscosities of saturated and compressed
fluid 1-chloro-1,2,2,2-tetrafluoroethane (R124) and pentafluoroethane (R125) at temperatures
between 120 and 420 K. Int J Thermophys 14(1):55–66
103. Dong X, Gong M, Shen J, Wu J (2011) Experimental measurement of vapor–liquid equilibrium for (trans-1,3,3,3-tetrafluoropropene (R1234ze(E))+propane (R290)). Int J Refrig
34(5):1238–1243
104. Dong X, Gong M, Shen J, Wu J (2012) Vapor–Liquid Equilibria of the trans-1,3,3,3Tetrafluoropropene (R1234ze(E)) + isobutane (R600a) system at various temperatures from
(258.150 to 288.150) K. J Chem Eng Data 57(2):541–544
105. Hu P, Chen L-X, Chen Z-S (2014) Vapor–liquid equilibria for binary system of 2,3,3,3tetrafluoroprop-1-ene (HFO-1234yf) +isobutane (HC-600a). Fluid Phase Equilib 365:1–4
106. Lim JS, Park J-Y, Lee B-G, Lee Y-W (2002) Phase equilibria of 1,1,1-trifluoroethane (HFC143a) + 1,1,1,2-tetrafluoroethane (HFC-134a), and + 1,1-difluoroethane (HFC-152a) at
273.15, 293.15, 303.15, and 313.15 K. Fluid Phase Equilib 193(1):29–39
107. Higashi Y (1999) Vapor−liquid equilibrium, coexistence curve, and critical locus for
pentafluoroethane + 1,1,1-trifluoroethane (R125/R143a). J Chem Eng Data 44:333–337
108. Nishiumi H, Akita H, Akiyama S (1997) High pressure vapor-liquid equilibria for the
HFC125-HFC152a system. Korean J Chem Eng 14(5):359–364
109. Higashi Y (1999) Vapor−liquid equilibrium, coexistence curve, and critical locus for pentafluoroethane + 1,1,1,2-tetrafluoroethane (R125/R134a). J Chem Eng Data 44(2):328–332
110. McLure IA, Edmonds B, Lal M (1973) Extremes in surface tension of fluorocarbon +
hydrocarbon mixtures. Nat Phys Sci 241(107):71–
111. Telo da Gama MM, Evans R (1983) The structure and surface tension of the liquid-vapour
interface near the upper critical end point of a binary mixture of Lennard-Jones fluids. Mol
Phys 48(2):229–50
112. Kohl AL, Nielsen RB (eds) (1997) Gas purification, 5th edn. Gulf Professional Publishing,
Houston, pp 40–186
113. Rochelle GT (2009) Amine scrubbing for CO 2 capture. Science 325(5948):1652
114. Puxty G, Maeder M (2016) 2—the fundamentals of post-combustion capture. In: Feron PHM
(ed) Absorption-based post-combustion capture of carbon dioxide: Woodhead Publishing pp
13–33
115. El Hadri N, Quang DV, Goetheer ELV, Abu Zahra MRM (2017) Aqueous amine solution
characterization for post-combustion CO 2 capture process. Appl Energy 185:1433–1449
116. Puxty G, Rowland R, Allport A, Yang Q, Bown M, Burns R, Maeder M, Attalla M
(2009) Carbon dioxide postcombustion capture: a novel screening study of the carbon
dioxide absorption performance of 76 amines (supporting information). Environ Sci Technol
43:6427–6433
117. Chowdhury FA, Yamada H, Higashii T, Goto K, Onoda M (2013) CO 2 capture by tertiary
amine absorbents: a performance comparison study. Ind Eng Chem Res 52:8323–8331
118. Rochelle G, Chen E, Freeman S, Van Wagener D, Xu Q, Voice A (2011) Aqueous piperazine
as the new standard for CO 2 capture technology. Chem Eng J 171(3):725–733
119. Liessmann G, Schmidt W, Reiffarth S (1995) Recommended thermodynamic data. Data
Compilation of the Saechsische Olefinwerke
L. F. Vega et al.
98. Llovell F, Pàmies JC, Vega LF (2004) Thermodynamic properties of Lennard-Jones chain
molecules: renormalization-group corrections to a modified statistical associating fluid theory.
J Chem Phys 121(21):10715–10724
99. Lemmon E, Huber M, McLinden M (2013) NIST standard reference database 23: reference
fluid thermodynamic and transport properties-REFPROP, version 9.1. Standard reference data
program. National Institute of Standards and Technology, Gaithersburg
100. Pádua AAH, Fareleira JMNA, Calado JCG, Wakeham WA (1996) Density and viscosity
measurements of 1,1,1,2-tetrafluoroethane (HFC-134a) from 199 K to 298 K and up to 100
MPa. J Chem Eng Data 41(4):731–735
101. Oliveira CMBP, Wakeham WA (1993) The viscosity of liquid R134a. Int J Thermophys
14(1):33–44
102. Diller DE, Peterson SM (1993) Measurements of the viscosities of saturated and compressed
fluid 1-chloro-1,2,2,2-tetrafluoroethane (R124) and pentafluoroethane (R125) at temperatures
between 120 and 420 K. Int J Thermophys 14(1):55–66
103. Dong X, Gong M, Shen J, Wu J (2011) Experimental measurement of vapor–liquid equilibrium for (trans-1,3,3,3-tetrafluoropropene (R1234ze(E))+propane (R290)). Int J Refrig
34(5):1238–1243
104. Dong X, Gong M, Shen J, Wu J (2012) Vapor–Liquid Equilibria of the trans-1,3,3,3Tetrafluoropropene (R1234ze(E)) + isobutane (R600a) system at various temperatures from
(258.150 to 288.150) K. J Chem Eng Data 57(2):541–544
105. Hu P, Chen L-X, Chen Z-S (2014) Vapor–liquid equilibria for binary system of 2,3,3,3tetrafluoroprop-1-ene (HFO-1234yf) +isobutane (HC-600a). Fluid Phase Equilib 365:1–4
106. Lim JS, Park J-Y, Lee B-G, Lee Y-W (2002) Phase equilibria of 1,1,1-trifluoroethane (HFC143a) + 1,1,1,2-tetrafluoroethane (HFC-134a), and + 1,1-difluoroethane (HFC-152a) at
273.15, 293.15, 303.15, and 313.15 K. Fluid Phase Equilib 193(1):29–39
107. Higashi Y (1999) Vapor−liquid equilibrium, coexistence curve, and critical locus for
pentafluoroethane + 1,1,1-trifluoroethane (R125/R143a). J Chem Eng Data 44:333–337
108. Nishiumi H, Akita H, Akiyama S (1997) High pressure vapor-liquid equilibria for the
HFC125-HFC152a system. Korean J Chem Eng 14(5):359–364
109. Higashi Y (1999) Vapor−liquid equilibrium, coexistence curve, and critical locus for pentafluoroethane + 1,1,1,2-tetrafluoroethane (R125/R134a). J Chem Eng Data 44(2):328–332
110. McLure IA, Edmonds B, Lal M (1973) Extremes in surface tension of fluorocarbon +
hydrocarbon mixtures. Nat Phys Sci 241(107):71–
111. Telo da Gama MM, Evans R (1983) The structure and surface tension of the liquid-vapour
interface near the upper critical end point of a binary mixture of Lennard-Jones fluids. Mol
Phys 48(2):229–50
112. Kohl AL, Nielsen RB (eds) (1997) Gas purification, 5th edn. Gulf Professional Publishing,
Houston, pp 40–186
113. Rochelle GT (2009) Amine scrubbing for CO 2 capture. Science 325(5948):1652
114. Puxty G, Maeder M (2016) 2—the fundamentals of post-combustion capture. In: Feron PHM
(ed) Absorption-based post-combustion capture of carbon dioxide: Woodhead Publishing pp
13–33
115. El Hadri N, Quang DV, Goetheer ELV, Abu Zahra MRM (2017) Aqueous amine solution
characterization for post-combustion CO 2 capture process. Appl Energy 185:1433–1449
116. Puxty G, Rowland R, Allport A, Yang Q, Bown M, Burns R, Maeder M, Attalla M
(2009) Carbon dioxide postcombustion capture: a novel screening study of the carbon
dioxide absorption performance of 76 amines (supporting information). Environ Sci Technol
43:6427–6433
117. Chowdhury FA, Yamada H, Higashii T, Goto K, Onoda M (2013) CO 2 capture by tertiary
amine absorbents: a performance comparison study. Ind Eng Chem Res 52:8323–8331
118. Rochelle G, Chen E, Freeman S, Van Wagener D, Xu Q, Voice A (2011) Aqueous piperazine
as the new standard for CO 2 capture technology. Chem Eng J 171(3):725–733
119. Liessmann G, Schmidt W, Reiffarth S (1995) Recommended thermodynamic data. Data
Compilation of the Saechsische Olefinwerke