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Binary liquid mixture
source: M. S. Reddy, et al., Thermochimica Acta, 630, 37 – 49, 2016
T=298 KP = 1 bar
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Binary liquid mixture of EmimBF4 and methoxyethanol
source: M. S. Reddy, et al., Thermochimica Acta, 630, 37 – 49, 2016
excess molar volume (mL/mol)
Vm= x1V1*+ (1−x1)V 2
*+x1(1−x1)(c+d x1)
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Binary liquid mixture of CS2 and acetone
source: Atkins, de Paula and Keeler, Physical Chemistry, 11ed., Figure 5A.13
Henry's law for aromatics in water at 25oC endothermic non-ideal mixing leads to phase separation
Molecular mass from osmotic pressuretriethylene glycol in water at 25oC
data from http://lpsb.nichd.nih.gov/tri_glycol.htm
line: 0.168 + 3.5X10-5
chap. 5 sect. C. binary vapor-liquid equilibrium
source: Dung T. Vu, et al., J. Chem. Eng. Data, 2006, 51, 1220-1225.
ethyl lactate and ethanol T = 40o C
chap. 5 sect. C. binary vapor-liquid equilibrium
source: Dung T. Vu, et al., J. Chem. Eng. Data, 2006, 51, 1220-1225.
mixtures of nitrogen and oxygen are nearly ideal
source: International Critical Tables
at fixed T
source: just a sketch
at fixed P
nitrogen and oxygen at 1 atma nearly-ideal mixture
negative deviation yields high-boiling azeotrope
positive deviation from ideality yields a low-boiling azeotrope
Source: The Phase Rule and Phase Relations,by Sydney T. Bowden, Macmillan & Co., 1950
Distillation cannot purify beyond the azeotrope. For example, ethanol and water cannot be distilled to greater than 96% ethanol.
less-than-ideal liquid-vapor equilibriummethanol and diethyl ether at T=303.15K
Baudilio Coto, et al., Journal of the Chemical Society Faraday Transactions, 91(24), 4381-4388, 1995.
less-than-ideal liquid-vapor equilibriummethanol and diethyl ether at T=303.15K
Baudilio Coto, et al., Journal of the Chemical Society Faraday Transactions, 91(24), 4381-4388, 1995.
At 50 kPa,yvapor = 0.407andxliquid = 0.855
Using the lever rule: If xmethanol =0.600, then thefraction of all moles that are in the liquid phase is
nliquid (0.600 - 0.407) = = 0.431 n (0.855 - 0.407)
less-than-ideal liquid-vapor equilibriummethanol and diethyl ether at T=303.15K
Baudilio Coto, et al., Journal of the Chemical Society Faraday Transactions, 91(24), 4381-4388, 1995.
At 50 kPa,yvapor = 0.407andxliquid = 0.855
5D. binary solid-liquid phase diagrams the case of no solid solution
eutectic point
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5D. binary solid-liquid phase diagrams the case of a compound that melts congruently
source: I. Ansara, et al., Calphad, 18(2), 177-222, 1994. Figure 12.DOI: 10.2475/ajs.s4-40.236.161
congruent melting
303K is themelting pointof Gallium
eutectic point
ternary phase diagrampolypropylene polyol (PPP) and water and methanol
Source: C. H. Lee, et al., Polymer, 146, 169-178, 2018
ternary phase diagrampolypropylene polyol (PPP) and water and methanol
Source: C. H. Lee, et al., Polymer, 146, 169-178, 2018
5F. Debye-Huckel limiting law (DHLL) 5F. Debye-Huckel limiting law
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