Mixture of Propylene Glycol + Water

Datasets

1. C_p,liquid - Molar heat capacity at constant pressure, J/K/mol (4)
2. η - Viscosity, Pa*s (8)
3. Excess molar heat capacity, J/K/mol (4)
4. P_vap - Vapor or sublimation pressure, kPa (2)
5. n₀ - Refractive index (Na D-line) (2)
6. ρ_l - Mass density, kg/m3 (16)
7. c_sound,fluid - Speed of Sound, m/s (6)
8. γ - Surface tension liquid-gas, N/m (2)
9. λ - Thermal conductivity, W/m/K (4)
10. T_fus - Solid-liquid equilibrium temperature, K (2)
11. v_spec - Specific volume, m3/kg (4)
12. Excess molar volume, m3/mol (6)

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational conditions:

• Pressure, kPa = 96.2 (Liquid)
• Mass fraction = 0.3 (Liquid)

Temperature, K - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
293.15	89.44
303.15	90.00
313.15	90.52
323.15	91.03

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Propylene Glycol (1) - Liquid	Temperature, K - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
0.2000	303.15	101.90
0.2000	313.15	103.00
0.2000	323.15	104.30
0.2000	333.15	105.80
0.2000	343.15	107.20
0.2000	353.15	108.80
0.4000	303.15	127.00
0.4000	313.15	129.40
0.4000	323.15	132.10
0.4000	333.15	134.90
0.4000	343.15	137.70
0.4000	353.15	140.70
0.5000	303.15	138.90
0.5000	313.15	141.90
0.5000	323.15	145.10
0.5000	333.15	148.70
0.5000	343.15	152.10
0.5000	353.15	155.60
0.6000	303.15	150.30
0.6000	313.15	153.90
0.6000	323.15	157.70
0.6000	333.15	161.80
0.6000	343.15	165.80
0.6000	353.15	169.90
0.8000	303.15	172.10
0.8000	313.15	176.40
0.8000	323.15	180.90
0.8000	333.15	185.80
0.8000	343.15	190.60
0.8000	353.15	195.50

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational conditions:

• Pressure, kPa = 96.2 (Liquid)
• Mass fraction = 0.3 (Liquid)

Temperature, K - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
293.15	89.44
303.15	90.00
313.15	90.52
323.15	91.03

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Propylene Glycol (1) - Liquid	Temperature, K - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
0.2000	303.15	101.90
0.2000	313.15	103.00
0.2000	323.15	104.30
0.2000	333.15	105.80
0.2000	343.15	107.20
0.2000	353.15	108.80
0.4000	303.15	127.00
0.4000	313.15	129.40
0.4000	323.15	132.10
0.4000	333.15	134.90
0.4000	343.15	137.70
0.4000	353.15	140.70
0.5000	303.15	138.90
0.5000	313.15	141.90
0.5000	323.15	145.10
0.5000	333.15	148.70
0.5000	343.15	152.10
0.5000	353.15	155.60
0.6000	303.15	150.30
0.6000	313.15	153.90
0.6000	323.15	157.70
0.6000	333.15	161.80
0.6000	343.15	165.80
0.6000	353.15	169.90
0.8000	303.15	172.10
0.8000	313.15	176.40
0.8000	323.15	180.90
0.8000	333.15	185.80
0.8000	343.15	190.60
0.8000	353.15	195.50

Viscosity, Pa*s [ref]

Operational conditions:

• Pressure, kPa = 96.2 (Liquid)
• Mass fraction = 0.3 (Liquid)

Temperature, K - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0030
303.15	0.0022
313.15	0.0016
323.15	0.0013

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mass fraction of Propylene Glycol (1) - Liquid	Viscosity, Pa*s - Liquid
273.15	0.0000	0.0018
273.15	0.0988	0.0029
273.15	0.1980	0.0046
273.15	0.3312	0.0087
273.15	0.5005	0.0191
273.15	0.6720	0.0402
273.15	0.8044	0.0750
273.15	0.9481	0.1691
273.15	1.0000	0.2580
283.15	0.0000	0.0013
283.15	0.0988	0.0020
283.15	0.1980	0.0030
283.15	0.3312	0.0053
283.15	0.5005	0.0108
283.15	0.6720	0.0212
283.15	0.8044	0.0384
283.15	0.9481	0.0867
283.15	1.0000	0.1167
293.15	0.0000	0.0010
293.15	0.0988	0.0015
293.15	0.1980	0.0022
293.15	0.3312	0.0035
293.15	0.5005	0.0067
293.15	0.6720	0.0126
293.15	0.8044	0.0217
293.15	0.9481	0.0457
293.15	1.0000	0.0597
303.15	0.0000	0.0008
303.15	0.0988	0.0011
303.15	0.1980	0.0016
303.15	0.3312	0.0025
303.15	0.5005	0.0045
303.15	0.6720	0.0080
303.15	0.8044	0.0133
303.15	0.9481	0.0261
303.15	1.0000	0.0333
313.15	0.0000	0.0007
313.15	0.0988	0.0009
313.15	0.1980	0.0012
313.15	0.3312	0.0019
313.15	0.5005	0.0032
313.15	0.6720	0.0054
313.15	0.8044	0.0086
313.15	0.9481	0.0160
313.15	1.0000	0.0199
323.15	0.0000	0.0006
323.15	0.0988	0.0008
323.15	0.1980	0.0010
323.15	0.3312	0.0014
323.15	0.5005	0.0023
323.15	0.6720	0.0039
323.15	0.8044	0.0059
323.15	0.9481	0.0104
323.15	1.0000	0.0127
333.15	0.0000	0.0005
333.15	0.0988	0.0006
333.15	0.1980	0.0008
333.15	0.3312	0.0011
333.15	0.5005	0.0018
333.15	0.6720	0.0029
333.15	0.8044	0.0042
333.15	0.9481	0.0071
333.15	1.0000	0.0085
343.15	0.0000	0.0004
343.15	0.0988	0.0005
343.15	0.1980	0.0007
343.15	0.3312	0.0009
343.15	0.5005	0.0014
343.15	0.6720	0.0022
343.15	0.8044	0.0032
343.15	0.9481	0.0051
343.15	1.0000	0.0059
353.15	0.0000	0.0004
353.15	0.0988	0.0005
353.15	0.1980	0.0006
353.15	0.3312	0.0008
353.15	0.5005	0.0012
353.15	0.6720	0.0017
353.15	0.8044	0.0024
353.15	0.9481	0.0037
353.15	1.0000	0.0043
253.15	0.5005	0.0849
253.15	0.6720	0.2044
253.15	0.8044	0.4157
253.15	0.9481	1.067
253.15	1.0000	1.7724
258.15	0.3312	0.0219
258.15	0.5005	0.0553
258.15	0.6720	0.1285
258.15	0.8044	0.2562
258.15	0.9481	0.6389
258.15	1.0000	1.0383
263.15	0.3312	0.0156
263.15	0.5005	0.0375
263.15	0.6720	0.0842
263.15	0.8044	0.1646
263.15	0.9481	0.3966
263.15	1.0000	0.6311
268.15	0.1980	0.0058
268.15	0.3312	0.0114
268.15	0.5005	0.0264
268.15	0.6720	0.0572
268.15	0.8044	0.1094
268.15	0.9481	0.2548
268.15	1.0000	0.3970

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0440	0.0412
298.15	0.0987	0.0384
298.15	0.1484	0.0357
298.15	0.2498	0.0302
298.15	0.3494	0.0248
298.15	0.4494	0.0197
298.15	0.5029	0.0171
298.15	0.5499	0.0150
298.15	0.5597	0.0146
298.15	0.6501	0.0108
298.15	0.7499	0.0073
298.15	0.8500	0.0043
298.15	0.9003	0.0030
298.15	0.9115	0.0028
298.15	0.9154	0.0027
298.15	0.9270	0.0024
298.15	0.9367	0.0022
298.15	0.9504	0.0019
298.15	0.9551	0.0018
298.15	0.9600	0.0017
298.15	0.9696	0.0015
298.15	0.9797	0.0013
298.15	0.9902	0.0011
298.15	0.9923	0.0010
298.15	0.9948	0.0010
308.15	0.0440	0.0230
308.15	0.0987	0.0214
308.15	0.1484	0.0199
308.15	0.2498	0.0168
308.15	0.3494	0.0138
308.15	0.4494	0.0109
308.15	0.5029	0.0095
308.15	0.5499	0.0083
308.15	0.5597	0.0080
308.15	0.6501	0.0060
308.15	0.7499	0.0040
308.15	0.8500	0.0025
308.15	0.9003	0.0018
308.15	0.9115	0.0017
308.15	0.9154	0.0016
308.15	0.9270	0.0015
308.15	0.9367	0.0014
308.15	0.9504	0.0012
308.15	0.9551	0.0012
308.15	0.9600	0.0011
308.15	0.9696	0.0010
308.15	0.9797	0.0009
308.15	0.9902	0.0008
308.15	0.9923	0.0008
308.15	0.9948	0.0008
318.15	0.0440	0.0121
318.15	0.0987	0.0113
318.15	0.1484	0.0105
318.15	0.2498	0.0089
318.15	0.3494	0.0073
318.15	0.4494	0.0059
318.15	0.5029	0.0052
318.15	0.5499	0.0046
318.15	0.5597	0.0045
318.15	0.6501	0.0036
318.15	0.7499	0.0027
318.15	0.8500	0.0019
318.15	0.9003	0.0015
318.15	0.9115	0.0014
318.15	0.9154	0.0013
318.15	0.9270	0.0012
318.15	0.9367	0.0012
318.15	0.9504	0.0010
318.15	0.9551	0.0010
318.15	0.9600	0.0010
318.15	0.9696	0.0009
318.15	0.9797	0.0008
318.15	0.9902	0.0007
318.15	0.9923	0.0007
318.15	0.9948	0.0006
328.15	0.0440	0.0092
328.15	0.0987	0.0086
328.15	0.1484	0.0080
328.15	0.2498	0.0069
328.15	0.3494	0.0058
328.15	0.4494	0.0048
328.15	0.5029	0.0043
328.15	0.5499	0.0039
328.15	0.5597	0.0038
328.15	0.6501	0.0030
328.15	0.7499	0.0021
328.15	0.8500	0.0014
328.15	0.9003	0.0010
328.15	0.9115	0.0009
328.15	0.9154	0.0009
328.15	0.9270	0.0008
328.15	0.9367	0.0008
328.15	0.9504	0.0007
328.15	0.9551	0.0007
328.15	0.9600	0.0007
328.15	0.9696	0.0006
328.15	0.9797	0.0006
328.15	0.9902	0.0005
328.15	0.9923	0.0005
328.15	0.9948	0.0005
338.15	0.0440	0.0067
338.15	0.0987	0.0063
338.15	0.1484	0.0059
338.15	0.2498	0.0051
338.15	0.3494	0.0044
338.15	0.4494	0.0037
338.15	0.5029	0.0033
338.15	0.5499	0.0030
338.15	0.5597	0.0030
338.15	0.6501	0.0024
338.15	0.7499	0.0018
338.15	0.8500	0.0012
338.15	0.9003	0.0009
338.15	0.9115	0.0008
338.15	0.9154	0.0008
338.15	0.9270	0.0007
338.15	0.9367	0.0007
338.15	0.9504	0.0006
338.15	0.9551	0.0006
338.15	0.9600	0.0006
338.15	0.9696	0.0006
338.15	0.9797	0.0005
338.15	0.9902	0.0005
338.15	0.9923	0.0005
338.15	0.9948	0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Mole fraction of Propylene Glycol (1) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.2500	296.65	0.0074
0.2500	313.05	0.0039
0.2500	333.10	0.0021
0.2500	353.05	0.0013
0.2500	363.30	0.0011
0.2500	373.45	0.0009
0.2500	384.15	0.0008
0.2500	394.55	0.0007
0.2500	411.75	0.0005
0.2500	429.55	0.0004
0.2500	449.55	0.0003
0.5000	297.05	0.0175
0.5000	313.05	0.0085
0.5000	333.10	0.0041
0.5000	353.10	0.0024
0.5000	363.40	0.0018
0.5000	383.50	0.0012
0.5000	398.75	0.0010
0.5000	411.45	0.0008
0.5000	428.95	0.0006
0.5000	443.95	0.0005
0.7500	296.80	0.0324
0.7500	313.05	0.0144
0.7500	333.10	0.0065
0.7500	353.05	0.0034
0.7500	363.35	0.0027
0.7500	378.35	0.0019
0.7500	388.50	0.0015
0.7500	398.30	0.0013
0.7500	408.15	0.0011

Viscosity, Pa*s [ref]

Operational conditions:

• Pressure, kPa = 96.2 (Liquid)
• Mass fraction = 0.3 (Liquid)

Temperature, K - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0030
303.15	0.0022
313.15	0.0016
323.15	0.0013

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mass fraction of Propylene Glycol (1) - Liquid	Viscosity, Pa*s - Liquid
273.15	0.0000	0.0018
273.15	0.0988	0.0029
273.15	0.1980	0.0046
273.15	0.3312	0.0087
273.15	0.5005	0.0191
273.15	0.6720	0.0402
273.15	0.8044	0.0750
273.15	0.9481	0.1691
273.15	1.0000	0.2580
283.15	0.0000	0.0013
283.15	0.0988	0.0020
283.15	0.1980	0.0030
283.15	0.3312	0.0053
283.15	0.5005	0.0108
283.15	0.6720	0.0212
283.15	0.8044	0.0384
283.15	0.9481	0.0867
283.15	1.0000	0.1167
293.15	0.0000	0.0010
293.15	0.0988	0.0015
293.15	0.1980	0.0022
293.15	0.3312	0.0035
293.15	0.5005	0.0067
293.15	0.6720	0.0126
293.15	0.8044	0.0217
293.15	0.9481	0.0457
293.15	1.0000	0.0597
303.15	0.0000	0.0008
303.15	0.0988	0.0011
303.15	0.1980	0.0016
303.15	0.3312	0.0025
303.15	0.5005	0.0045
303.15	0.6720	0.0080
303.15	0.8044	0.0133
303.15	0.9481	0.0261
303.15	1.0000	0.0333
313.15	0.0000	0.0007
313.15	0.0988	0.0009
313.15	0.1980	0.0012
313.15	0.3312	0.0019
313.15	0.5005	0.0032
313.15	0.6720	0.0054
313.15	0.8044	0.0086
313.15	0.9481	0.0160
313.15	1.0000	0.0199
323.15	0.0000	0.0006
323.15	0.0988	0.0008
323.15	0.1980	0.0010
323.15	0.3312	0.0014
323.15	0.5005	0.0023
323.15	0.6720	0.0039
323.15	0.8044	0.0059
323.15	0.9481	0.0104
323.15	1.0000	0.0127
333.15	0.0000	0.0005
333.15	0.0988	0.0006
333.15	0.1980	0.0008
333.15	0.3312	0.0011
333.15	0.5005	0.0018
333.15	0.6720	0.0029
333.15	0.8044	0.0042
333.15	0.9481	0.0071
333.15	1.0000	0.0085
343.15	0.0000	0.0004
343.15	0.0988	0.0005
343.15	0.1980	0.0007
343.15	0.3312	0.0009
343.15	0.5005	0.0014
343.15	0.6720	0.0022
343.15	0.8044	0.0032
343.15	0.9481	0.0051
343.15	1.0000	0.0059
353.15	0.0000	0.0004
353.15	0.0988	0.0005
353.15	0.1980	0.0006
353.15	0.3312	0.0008
353.15	0.5005	0.0012
353.15	0.6720	0.0017
353.15	0.8044	0.0024
353.15	0.9481	0.0037
353.15	1.0000	0.0043
253.15	0.5005	0.0849
253.15	0.6720	0.2044
253.15	0.8044	0.4157
253.15	0.9481	1.067
253.15	1.0000	1.7724
258.15	0.3312	0.0219
258.15	0.5005	0.0553
258.15	0.6720	0.1285
258.15	0.8044	0.2562
258.15	0.9481	0.6389
258.15	1.0000	1.0383
263.15	0.3312	0.0156
263.15	0.5005	0.0375
263.15	0.6720	0.0842
263.15	0.8044	0.1646
263.15	0.9481	0.3966
263.15	1.0000	0.6311
268.15	0.1980	0.0058
268.15	0.3312	0.0114
268.15	0.5005	0.0264
268.15	0.6720	0.0572
268.15	0.8044	0.1094
268.15	0.9481	0.2548
268.15	1.0000	0.3970

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0440	0.0412
298.15	0.0987	0.0384
298.15	0.1484	0.0357
298.15	0.2498	0.0302
298.15	0.3494	0.0248
298.15	0.4494	0.0197
298.15	0.5029	0.0171
298.15	0.5499	0.0150
298.15	0.5597	0.0146
298.15	0.6501	0.0108
298.15	0.7499	0.0073
298.15	0.8500	0.0043
298.15	0.9003	0.0030
298.15	0.9115	0.0028
298.15	0.9154	0.0027
298.15	0.9270	0.0024
298.15	0.9367	0.0022
298.15	0.9504	0.0019
298.15	0.9551	0.0018
298.15	0.9600	0.0017
298.15	0.9696	0.0015
298.15	0.9797	0.0013
298.15	0.9902	0.0011
298.15	0.9923	0.0010
298.15	0.9948	0.0010
308.15	0.0440	0.0230
308.15	0.0987	0.0214
308.15	0.1484	0.0199
308.15	0.2498	0.0168
308.15	0.3494	0.0138
308.15	0.4494	0.0109
308.15	0.5029	0.0095
308.15	0.5499	0.0083
308.15	0.5597	0.0080
308.15	0.6501	0.0060
308.15	0.7499	0.0040
308.15	0.8500	0.0025
308.15	0.9003	0.0018
308.15	0.9115	0.0017
308.15	0.9154	0.0016
308.15	0.9270	0.0015
308.15	0.9367	0.0014
308.15	0.9504	0.0012
308.15	0.9551	0.0012
308.15	0.9600	0.0011
308.15	0.9696	0.0010
308.15	0.9797	0.0009
308.15	0.9902	0.0008
308.15	0.9923	0.0008
308.15	0.9948	0.0008
318.15	0.0440	0.0121
318.15	0.0987	0.0113
318.15	0.1484	0.0105
318.15	0.2498	0.0089
318.15	0.3494	0.0073
318.15	0.4494	0.0059
318.15	0.5029	0.0052
318.15	0.5499	0.0046
318.15	0.5597	0.0045
318.15	0.6501	0.0036
318.15	0.7499	0.0027
318.15	0.8500	0.0019
318.15	0.9003	0.0015
318.15	0.9115	0.0014
318.15	0.9154	0.0013
318.15	0.9270	0.0012
318.15	0.9367	0.0012
318.15	0.9504	0.0010
318.15	0.9551	0.0010
318.15	0.9600	0.0010
318.15	0.9696	0.0009
318.15	0.9797	0.0008
318.15	0.9902	0.0007
318.15	0.9923	0.0007
318.15	0.9948	0.0006
328.15	0.0440	0.0092
328.15	0.0987	0.0086
328.15	0.1484	0.0080
328.15	0.2498	0.0069
328.15	0.3494	0.0058
328.15	0.4494	0.0048
328.15	0.5029	0.0043
328.15	0.5499	0.0039
328.15	0.5597	0.0038
328.15	0.6501	0.0030
328.15	0.7499	0.0021
328.15	0.8500	0.0014
328.15	0.9003	0.0010
328.15	0.9115	0.0009
328.15	0.9154	0.0009
328.15	0.9270	0.0008
328.15	0.9367	0.0008
328.15	0.9504	0.0007
328.15	0.9551	0.0007
328.15	0.9600	0.0007
328.15	0.9696	0.0006
328.15	0.9797	0.0006
328.15	0.9902	0.0005
328.15	0.9923	0.0005
328.15	0.9948	0.0005
338.15	0.0440	0.0067
338.15	0.0987	0.0063
338.15	0.1484	0.0059
338.15	0.2498	0.0051
338.15	0.3494	0.0044
338.15	0.4494	0.0037
338.15	0.5029	0.0033
338.15	0.5499	0.0030
338.15	0.5597	0.0030
338.15	0.6501	0.0024
338.15	0.7499	0.0018
338.15	0.8500	0.0012
338.15	0.9003	0.0009
338.15	0.9115	0.0008
338.15	0.9154	0.0008
338.15	0.9270	0.0007
338.15	0.9367	0.0007
338.15	0.9504	0.0006
338.15	0.9551	0.0006
338.15	0.9600	0.0006
338.15	0.9696	0.0006
338.15	0.9797	0.0005
338.15	0.9902	0.0005
338.15	0.9923	0.0005
338.15	0.9948	0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Mole fraction of Propylene Glycol (1) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.2500	296.65	0.0074
0.2500	313.05	0.0039
0.2500	333.10	0.0021
0.2500	353.05	0.0013
0.2500	363.30	0.0011
0.2500	373.45	0.0009
0.2500	384.15	0.0008
0.2500	394.55	0.0007
0.2500	411.75	0.0005
0.2500	429.55	0.0004
0.2500	449.55	0.0003
0.5000	297.05	0.0175
0.5000	313.05	0.0085
0.5000	333.10	0.0041
0.5000	353.10	0.0024
0.5000	363.40	0.0018
0.5000	383.50	0.0012
0.5000	398.75	0.0010
0.5000	411.45	0.0008
0.5000	428.95	0.0006
0.5000	443.95	0.0005
0.7500	296.80	0.0324
0.7500	313.05	0.0144
0.7500	333.10	0.0065
0.7500	353.05	0.0034
0.7500	363.35	0.0027
0.7500	378.35	0.0019
0.7500	388.50	0.0015
0.7500	398.30	0.0013
0.7500	408.15	0.0011

Excess molar heat capacity, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propylene Glycol (1) - Liquid	Excess molar heat capacity, J/K/mol - Liquid
283.15	0.0222	1.78
283.15	0.0562	3.3
283.15	0.0785	4.67
283.15	0.1224	5.38
283.15	0.1545	5.22
283.15	0.1667	4.94
283.15	0.1873	4.62
283.15	0.2272	4.15
283.15	0.2878	2.67
283.15	0.3965	1.6
283.15	0.4863	0.6700
283.15	0.5274	0.6900
283.15	0.6388	0.7700
283.15	0.7530	0.7200
283.15	0.7757	0.8000
283.15	0.9045	0.2600
283.15	0.9677	0.0900
293.15	0.0222	2.01
293.15	0.0562	3.57
293.15	0.0785	5.18
293.15	0.1224	6.18
293.15	0.1545	6.19
293.15	0.1667	6.02
293.15	0.1873	5.79
293.15	0.2272	5.41
293.15	0.2878	4.01
293.15	0.3965	3.11
293.15	0.4863	1.88
293.15	0.5274	1.74
293.15	0.6388	1.63
293.15	0.7530	1.32
293.15	0.7757	1.04
293.15	0.9045	0.3800
293.15	0.9677	-0.0800
298.15	0.0222	1.98
298.15	0.0562	3.62
298.15	0.0785	5.29
298.15	0.1224	6.43
298.15	0.1545	6.5
298.15	0.1667	6.37
298.15	0.1873	6.18
298.15	0.2272	5.86
298.15	0.2878	4.52
298.15	0.3965	3.65
298.15	0.4863	2.34
298.15	0.5274	2.17
298.15	0.6388	1.97
298.15	0.7530	1.55
298.15	0.7757	1.24
298.15	0.9045	0.1100
298.15	0.9677	-0.1300
303.15	0.0222	1.95
303.15	0.0562	3.63
303.15	0.0785	5.35
303.15	0.1224	6.6
303.15	0.1545	6.73
303.15	0.1667	6.62
303.15	0.1873	6.49
303.15	0.2272	6.21
303.15	0.2878	4.94
303.15	0.3965	4.08
303.15	0.4863	2.75
303.15	0.5274	2.58
303.15	0.6388	2.3
303.15	0.7530	1.76
303.15	0.7757	1.47
303.15	0.9045	0.1400
303.15	0.9677	-0.1500
313.15	0.0222	1.84
313.15	0.0562	3.59
313.15	0.0785	5.39
313.15	0.1224	6.81
313.15	0.1545	6.96
313.15	0.1667	6.95
313.15	0.1873	6.9
313.15	0.2272	6.72
313.15	0.2878	5.62
313.15	0.3965	4.77
313.15	0.4863	3.53
313.15	0.5274	3.35
313.15	0.6388	3.01
313.15	0.7530	2.18
313.15	0.7757	1.96
313.15	0.9045	0.3200
313.15	0.9677	-0.0600

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propylene Glycol (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15	0.0266	-0.2790
298.15	0.0579	-0.5620
298.15	0.1214	-0.8780
298.15	0.2050	-0.9700
298.15	0.3040	-0.9130
298.15	0.3872	-0.8370
298.15	0.4957	-0.7020
298.15	0.5454	-0.6350
298.15	0.6431	-0.5420
298.15	0.7386	-0.4360
298.15	0.8236	-0.3250
298.15	0.9233	-0.1500
323.15	0.0266	-0.2270
323.15	0.0579	-0.3930
323.15	0.1214	-0.6280
323.15	0.2050	-0.7530
323.15	0.3040	-0.7460
323.15	0.3872	-0.7250
323.15	0.4957	-0.6430
323.15	0.5454	-0.6020
323.15	0.6431	-0.5080
323.15	0.7386	-0.3960
323.15	0.8236	-0.2790
323.15	0.9233	-0.1300
343.15	0.0266	-0.1440
343.15	0.0579	-0.2830
343.15	0.1214	-0.4620
343.15	0.2050	-0.5030
343.15	0.3040	-0.5140
343.15	0.3872	-0.4990
343.15	0.4957	-0.4530
343.15	0.5454	-0.4250
343.15	0.6431	-0.3680
343.15	0.7386	-0.2930
343.15	0.8236	-0.2160
343.15	0.9233	-0.1190

Excess molar heat capacity, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propylene Glycol (1) - Liquid	Excess molar heat capacity, J/K/mol - Liquid
283.15	0.0222	1.78
283.15	0.0562	3.3
283.15	0.0785	4.67
283.15	0.1224	5.38
283.15	0.1545	5.22
283.15	0.1667	4.94
283.15	0.1873	4.62
283.15	0.2272	4.15
283.15	0.2878	2.67
283.15	0.3965	1.6
283.15	0.4863	0.6700
283.15	0.5274	0.6900
283.15	0.6388	0.7700
283.15	0.7530	0.7200
283.15	0.7757	0.8000
283.15	0.9045	0.2600
283.15	0.9677	0.0900
293.15	0.0222	2.01
293.15	0.0562	3.57
293.15	0.0785	5.18
293.15	0.1224	6.18
293.15	0.1545	6.19
293.15	0.1667	6.02
293.15	0.1873	5.79
293.15	0.2272	5.41
293.15	0.2878	4.01
293.15	0.3965	3.11
293.15	0.4863	1.88
293.15	0.5274	1.74
293.15	0.6388	1.63
293.15	0.7530	1.32
293.15	0.7757	1.04
293.15	0.9045	0.3800
293.15	0.9677	-0.0800
298.15	0.0222	1.98
298.15	0.0562	3.62
298.15	0.0785	5.29
298.15	0.1224	6.43
298.15	0.1545	6.5
298.15	0.1667	6.37
298.15	0.1873	6.18
298.15	0.2272	5.86
298.15	0.2878	4.52
298.15	0.3965	3.65
298.15	0.4863	2.34
298.15	0.5274	2.17
298.15	0.6388	1.97
298.15	0.7530	1.55
298.15	0.7757	1.24
298.15	0.9045	0.1100
298.15	0.9677	-0.1300
303.15	0.0222	1.95
303.15	0.0562	3.63
303.15	0.0785	5.35
303.15	0.1224	6.6
303.15	0.1545	6.73
303.15	0.1667	6.62
303.15	0.1873	6.49
303.15	0.2272	6.21
303.15	0.2878	4.94
303.15	0.3965	4.08
303.15	0.4863	2.75
303.15	0.5274	2.58
303.15	0.6388	2.3
303.15	0.7530	1.76
303.15	0.7757	1.47
303.15	0.9045	0.1400
303.15	0.9677	-0.1500
313.15	0.0222	1.84
313.15	0.0562	3.59
313.15	0.0785	5.39
313.15	0.1224	6.81
313.15	0.1545	6.96
313.15	0.1667	6.95
313.15	0.1873	6.9
313.15	0.2272	6.72
313.15	0.2878	5.62
313.15	0.3965	4.77
313.15	0.4863	3.53
313.15	0.5274	3.35
313.15	0.6388	3.01
313.15	0.7530	2.18
313.15	0.7757	1.96
313.15	0.9045	0.3200
313.15	0.9677	-0.0600

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propylene Glycol (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15	0.0266	-0.2790
298.15	0.0579	-0.5620
298.15	0.1214	-0.8780
298.15	0.2050	-0.9700
298.15	0.3040	-0.9130
298.15	0.3872	-0.8370
298.15	0.4957	-0.7020
298.15	0.5454	-0.6350
298.15	0.6431	-0.5420
298.15	0.7386	-0.4360
298.15	0.8236	-0.3250
298.15	0.9233	-0.1500
323.15	0.0266	-0.2270
323.15	0.0579	-0.3930
323.15	0.1214	-0.6280
323.15	0.2050	-0.7530
323.15	0.3040	-0.7460
323.15	0.3872	-0.7250
323.15	0.4957	-0.6430
323.15	0.5454	-0.6020
323.15	0.6431	-0.5080
323.15	0.7386	-0.3960
323.15	0.8236	-0.2790
323.15	0.9233	-0.1300
343.15	0.0266	-0.1440
343.15	0.0579	-0.2830
343.15	0.1214	-0.4620
343.15	0.2050	-0.5030
343.15	0.3040	-0.5140
343.15	0.3872	-0.4990
343.15	0.4957	-0.4530
343.15	0.5454	-0.4250
343.15	0.6431	-0.3680
343.15	0.7386	-0.2930
343.15	0.8236	-0.2160
343.15	0.9233	-0.1190

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
345.15	0.0000	0.62
347.15	0.0000	0.70
350.15	0.0000	0.84
353.15	0.0000	1.00
355.15	0.0000	1.13
357.15	0.0000	1.27
360.15	0.0000	1.51
363.15	0.0000	1.78
365.15	0.0000	1.99
367.15	0.0000	2.21
370.15	0.0000	2.60
373.15	0.0000	3.03
375.15	0.0000	3.36
377.15	0.0000	3.72
347.15	0.2710	11.27
350.15	0.2710	12.93
353.15	0.2710	14.74
355.15	0.2710	16.00
357.15	0.2710	17.21
360.15	0.2710	19.14
363.15	0.2710	21.61
365.15	0.2710	23.61
367.15	0.2710	25.38
370.15	0.2710	28.06
373.15	0.2710	31.26
375.15	0.2710	33.62
330.15	0.5030	9.32
333.15	0.5030	10.70
335.15	0.5030	11.71
337.15	0.5030	12.81
340.15	0.5030	14.69
343.15	0.5030	16.87
345.15	0.5030	18.47
347.15	0.5030	20.21
350.15	0.5030	22.92
353.15	0.5030	25.78
355.15	0.5030	27.88
360.15	0.5030	34.15
323.15	0.7012	9.03
325.15	0.7012	9.99
327.15	0.7012	11.02
330.15	0.7012	12.66
333.15	0.7012	14.53
335.15	0.7012	15.91
337.15	0.7012	17.47
340.15	0.7012	20.03
343.15	0.7012	22.89
345.15	0.7012	24.98
347.15	0.7012	27.23
350.15	0.7012	30.96
323.15	0.9018	11.09
325.15	0.9018	12.30
327.15	0.9018	13.58
330.15	0.9018	15.58
333.15	0.9018	17.70
335.15	0.9018	19.42
337.15	0.9018	21.61
340.15	0.9018	24.87
343.15	0.9018	28.32
345.15	0.9018	30.85
347.15	0.9018	33.52
317.15	1.0000	9.11
320.15	1.0000	10.63
323.15	1.0000	12.35
325.15	1.0000	13.63
327.15	1.0000	15.02
330.15	1.0000	17.33
333.15	1.0000	19.94
335.15	1.0000	21.86
337.15	1.0000	23.93
340.15	1.0000	27.35
343.15	1.0000	31.18
345.15	1.0000	33.98

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
345.15	0.0000	0.62
347.15	0.0000	0.70
350.15	0.0000	0.84
353.15	0.0000	1.00
355.15	0.0000	1.13
357.15	0.0000	1.27
360.15	0.0000	1.51
363.15	0.0000	1.78
365.15	0.0000	1.99
367.15	0.0000	2.21
370.15	0.0000	2.60
373.15	0.0000	3.03
375.15	0.0000	3.36
377.15	0.0000	3.72
347.15	0.2710	11.27
350.15	0.2710	12.93
353.15	0.2710	14.74
355.15	0.2710	16.00
357.15	0.2710	17.21
360.15	0.2710	19.14
363.15	0.2710	21.61
365.15	0.2710	23.61
367.15	0.2710	25.38
370.15	0.2710	28.06
373.15	0.2710	31.26
375.15	0.2710	33.62
330.15	0.5030	9.32
333.15	0.5030	10.70
335.15	0.5030	11.71
337.15	0.5030	12.81
340.15	0.5030	14.69
343.15	0.5030	16.87
345.15	0.5030	18.47
347.15	0.5030	20.21
350.15	0.5030	22.92
353.15	0.5030	25.78
355.15	0.5030	27.88
360.15	0.5030	34.15
323.15	0.7012	9.03
325.15	0.7012	9.99
327.15	0.7012	11.02
330.15	0.7012	12.66
333.15	0.7012	14.53
335.15	0.7012	15.91
337.15	0.7012	17.47
340.15	0.7012	20.03
343.15	0.7012	22.89
345.15	0.7012	24.98
347.15	0.7012	27.23
350.15	0.7012	30.96
323.15	0.9018	11.09
325.15	0.9018	12.30
327.15	0.9018	13.58
330.15	0.9018	15.58
333.15	0.9018	17.70
335.15	0.9018	19.42
337.15	0.9018	21.61
340.15	0.9018	24.87
343.15	0.9018	28.32
345.15	0.9018	30.85
347.15	0.9018	33.52
317.15	1.0000	9.11
320.15	1.0000	10.63
323.15	1.0000	12.35
325.15	1.0000	13.63
327.15	1.0000	15.02
330.15	1.0000	17.33
333.15	1.0000	19.94
335.15	1.0000	21.86
337.15	1.0000	23.93
340.15	1.0000	27.35
343.15	1.0000	31.18
345.15	1.0000	33.98

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mass fraction of Propylene Glycol (1) - Liquid	Refractive index (Na D-line) - Liquid
278.15	0.0000	1.3341
278.15	0.0988	1.3458
278.15	0.1980	1.3578
278.15	0.3312	1.374
278.15	0.5005	1.3946
278.15	0.6720	1.4112
278.15	0.8044	1.4231
278.15	0.9481	1.4343
278.15	1.0000	1.438
283.15	0.0000	1.3338
283.15	0.0988	1.3454
283.15	0.1980	1.3571
283.15	0.3312	1.373
283.15	0.5005	1.3932
283.15	0.6720	1.4098
283.15	0.8044	1.4216
283.15	0.9481	1.4328
283.15	1.0000	1.4364
288.15	0.0000	1.3335
288.15	0.0988	1.3449
288.15	0.1980	1.3564
288.15	0.3312	1.372
288.15	0.5005	1.3918
288.15	0.6720	1.4084
288.15	0.8044	1.42
288.15	0.9481	1.4312
288.15	1.0000	1.4348
293.15	0.0000	1.3331
293.15	0.0988	1.3444
293.15	0.1980	1.3557
293.15	0.3312	1.371
293.15	0.5005	1.3903
293.15	0.6720	1.4069
293.15	0.8044	1.4184
293.15	0.9481	1.4296
293.15	1.0000	1.4332
298.15	0.0000	1.3326
298.15	0.0988	1.3432
298.15	0.1980	1.355
298.15	0.3312	1.3699
298.15	0.5005	1.3889
298.15	0.6720	1.4054
298.15	0.8044	1.4168
298.15	0.9481	1.428
298.15	1.0000	1.4315
303.15	0.0000	1.332
303.15	0.0988	1.3432
303.15	0.1980	1.3542
303.15	0.3312	1.3689
303.15	0.5005	1.3874
303.15	0.6720	1.4039
303.15	0.8044	1.415
303.15	0.9481	1.4264
303.15	1.0000	1.4299
308.15	0.0000	1.3313
308.15	0.0988	1.3424
308.15	0.1980	1.3534
308.15	0.3312	1.368
308.15	0.5005	1.3862
308.15	0.6720	1.4024
308.15	0.8044	1.4135
308.15	0.9481	1.4248
308.15	1.0000	1.4281
313.15	0.0000	1.3306
313.15	0.0988	1.3416
313.15	0.1980	1.3534
313.15	0.3312	1.3671
313.15	0.5005	1.3851
313.15	0.6720	1.4008
313.15	0.8044	1.4119
313.15	0.9481	1.4231
313.15	1.0000	1.4264
318.15	0.0000	1.3298
318.15	0.0988	1.3408
318.15	0.1980	1.3516
318.15	0.3312	1.366
318.15	0.5005	1.384
318.15	0.6720	1.3994
318.15	0.8044	1.4103
318.15	0.9481	1.4214
318.15	1.0000	1.4247

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mass fraction of Propylene Glycol (1) - Liquid	Refractive index (Na D-line) - Liquid
278.15	0.0000	1.3341
278.15	0.0988	1.3458
278.15	0.1980	1.3578
278.15	0.3312	1.374
278.15	0.5005	1.3946
278.15	0.6720	1.4112
278.15	0.8044	1.4231
278.15	0.9481	1.4343
278.15	1.0000	1.438
283.15	0.0000	1.3338
283.15	0.0988	1.3454
283.15	0.1980	1.3571
283.15	0.3312	1.373
283.15	0.5005	1.3932
283.15	0.6720	1.4098
283.15	0.8044	1.4216
283.15	0.9481	1.4328
283.15	1.0000	1.4364
288.15	0.0000	1.3335
288.15	0.0988	1.3449
288.15	0.1980	1.3564
288.15	0.3312	1.372
288.15	0.5005	1.3918
288.15	0.6720	1.4084
288.15	0.8044	1.42
288.15	0.9481	1.4312
288.15	1.0000	1.4348
293.15	0.0000	1.3331
293.15	0.0988	1.3444
293.15	0.1980	1.3557
293.15	0.3312	1.371
293.15	0.5005	1.3903
293.15	0.6720	1.4069
293.15	0.8044	1.4184
293.15	0.9481	1.4296
293.15	1.0000	1.4332
298.15	0.0000	1.3326
298.15	0.0988	1.3432
298.15	0.1980	1.355
298.15	0.3312	1.3699
298.15	0.5005	1.3889
298.15	0.6720	1.4054
298.15	0.8044	1.4168
298.15	0.9481	1.428
298.15	1.0000	1.4315
303.15	0.0000	1.332
303.15	0.0988	1.3432
303.15	0.1980	1.3542
303.15	0.3312	1.3689
303.15	0.5005	1.3874
303.15	0.6720	1.4039
303.15	0.8044	1.415
303.15	0.9481	1.4264
303.15	1.0000	1.4299
308.15	0.0000	1.3313
308.15	0.0988	1.3424
308.15	0.1980	1.3534
308.15	0.3312	1.368
308.15	0.5005	1.3862
308.15	0.6720	1.4024
308.15	0.8044	1.4135
308.15	0.9481	1.4248
308.15	1.0000	1.4281
313.15	0.0000	1.3306
313.15	0.0988	1.3416
313.15	0.1980	1.3534
313.15	0.3312	1.3671
313.15	0.5005	1.3851
313.15	0.6720	1.4008
313.15	0.8044	1.4119
313.15	0.9481	1.4231
313.15	1.0000	1.4264
318.15	0.0000	1.3298
318.15	0.0988	1.3408
318.15	0.1980	1.3516
318.15	0.3312	1.366
318.15	0.5005	1.384
318.15	0.6720	1.3994
318.15	0.8044	1.4103
318.15	0.9481	1.4214
318.15	1.0000	1.4247

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propylene Glycol (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	997.05
298.15	0.0500	1011.79
298.15	0.1000	1022.73
298.15	0.1500	1030.33
298.15	0.2000	1035.27
298.15	0.2500	1038.27
298.15	0.3000	1039.85
298.15	0.3500	1040.55
298.15	0.4000	1040.6
298.15	0.4500	1040.28
298.15	0.5000	1039.83
298.15	0.5500	1039.24
298.15	0.6000	1038.53
298.15	0.6500	1037.84
298.15	0.7000	1037.09
298.15	0.7500	1036.33
298.15	0.8000	1035.57
298.15	0.8500	1034.81
298.15	0.9000	1034.08
298.15	0.9500	1033.35
298.15	1.0000	1032.69
308.15	0.0000	994.03
308.15	0.0500	1007.53
308.15	0.1000	1017.48
308.15	0.1500	1024.23
308.15	0.2000	1028.47
308.15	0.2500	1031.17
308.15	0.3000	1032.55
308.15	0.3500	1033.05
308.15	0.4000	1033.02
308.15	0.4500	1032.76
308.15	0.5000	1032.3
308.15	0.5500	1031.7
308.15	0.6000	1031.03
308.15	0.6500	1030.31
308.15	0.7000	1029.56
308.15	0.7500	1028.81
308.15	0.8000	1028.06
308.15	0.8500	1027.32
308.15	0.9000	1026.59
308.15	0.9500	1025.88
308.15	1.0000	1025.21
318.15	0.0000	990.16
318.15	0.0500	1002.61
318.15	0.1000	1011.69
318.15	0.1500	1017.73
318.15	0.2000	1021.65
318.15	0.2500	1023.85
318.15	0.3000	1025.01
318.15	0.3500	1025.42
318.15	0.4000	1025.34
318.15	0.4500	1025.05
318.15	0.5000	1024.54
318.15	0.5500	1023.93
318.15	0.6000	1023.29
318.15	0.6500	1022.58
318.15	0.7000	1021.87
318.15	0.7500	1021.11
318.15	0.8000	1020.37
318.15	0.8500	1019.61
318.15	0.9000	1018.9
318.15	0.9500	1018.19
318.15	1.0000	1017.51
328.15	0.0000	985.66
328.15	0.0500	997.16
328.15	0.1000	1005.39
328.15	0.1500	1010.88
328.15	0.2000	1014.32
328.15	0.2500	1016.27
328.15	0.3000	1017.25
328.15	0.3500	1017.54
328.15	0.4000	1017.47
328.15	0.4500	1017.1
328.15	0.5000	1016.59
328.15	0.5500	1016.0
328.15	0.6000	1015.39
328.15	0.6500	1014.69
328.15	0.7000	1014.0
328.15	0.7500	1013.3
328.15	0.8000	1012.54
328.15	0.8500	1011.8
328.15	0.9000	1011.06
328.15	0.9500	1010.37
328.15	1.0000	1009.78

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Molality, mol/kg of Water (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	1032.87
0.2187	1033.12
0.5592	1033.53
0.6141	1033.58
0.7341	1033.67
0.8421	1033.73
0.9215	1033.86
1.0234	1033.94

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Propylene Glycol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0731	1016.4
0.1555	1031.1
0.2449	1037.7
0.3384	1039.6
0.4321	1039.8
0.5223	1039.0
0.6058	1038.0
0.6803	1036.8
0.7446	1035.9
0.7987	1035.0
0.8430	1034.5
0.8786	1033.8
0.9068	1033.4
0.9355	1033.1

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 96.2 (Liquid)
• Mass fraction = 0.3 (Liquid)

Temperature, K - Liquid	Mass density, kg/m3 - Liquid
293.15	1023.1
303.15	1019.2
313.15	1014.5
323.15	1009.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mass fraction of Propylene Glycol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.2500	1020.98
293.15	0.2500	1019.08
298.15	0.2500	1017.01
303.15	0.2500	1014.78
308.15	0.2500	1012.38
313.15	0.2500	1009.84
318.15	0.2500	1007.15
288.15	0.5000	1041.16
293.15	0.5000	1038.02
298.15	0.5000	1034.79
303.15	0.5000	1031.49
308.15	0.5000	1028.11
313.15	0.5000	1024.66
318.15	0.5000	1021.13
288.15	0.7500	1047.67
293.15	0.7500	1044.04
298.15	0.7500	1040.37
303.15	0.7500	1036.64
308.15	0.7500	1032.88
313.15	0.7500	1029.06
318.15	0.7500	1025.19
288.15	0.2500	1020.99
293.15	0.2500	1019.1
298.15	0.2500	1017.02
303.15	0.2500	1014.79
308.15	0.2500	1012.39
313.15	0.2500	1009.85
293.15	0.2500	1019.09
298.15	0.7500	1040.36
308.15	0.7500	1032.87
313.15	0.7500	1029.05
293.15	0.5000	1038.01
298.15	0.5000	1034.78
303.15	0.5000	1031.48
313.15	0.5000	1024.65
318.15	0.5000	1021.12

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mass fraction of Propylene Glycol (1) - Liquid	Mass density, kg/m3 - Liquid
273.15	0.0000	1000.8
273.15	0.0988	1009.8
273.15	0.1980	1020.8
273.15	0.3312	1036.3
273.15	0.5005	1051.1
273.15	0.6720	1057.5
273.15	0.8044	1057.6
273.15	0.9481	1053.8
273.15	1.0000	1051.3
283.15	0.0000	1000.6
283.15	0.0988	1008.2
283.15	0.1980	1017.8
283.15	0.3312	1031.2
283.15	0.5005	1044.6
283.15	0.6720	1050.5
283.15	0.8044	1050.4
283.15	0.9481	1045.6
283.15	1.0000	1042.9
293.15	0.0000	999.3
293.15	0.0988	1005.7
293.15	0.1980	1014.5
293.15	0.3312	1026.3
293.15	0.5005	1038.1
293.15	0.6720	1043.2
293.15	0.8044	1042.9
293.15	0.9481	1038.2
293.15	1.0000	1035.5
303.15	0.0000	996.8
303.15	0.0988	1002.6
303.15	0.1980	1010.6
303.15	0.3312	1021.0
303.15	0.5005	1031.4
303.15	0.6720	1035.9
303.15	0.8044	1035.4
303.15	0.9481	1030.8
303.15	1.0000	1028.1
313.15	0.0000	993.2
313.15	0.0988	999.0
313.15	0.1980	1006.0
313.15	0.3312	1015.3
313.15	0.5005	1024.5
313.15	0.6720	1028.4
313.15	0.8044	1027.8
313.15	0.9481	1023.2
313.15	1.0000	1020.6
323.15	0.0000	989.0
323.15	0.0988	994.4
323.15	0.1980	1000.8
323.15	0.3312	1009.2
323.15	0.5005	1017.4
323.15	0.6720	1020.8
323.15	0.8044	1020.1
323.15	0.9481	1015.6
323.15	1.0000	1013.0
333.15	0.0000	984.4
333.15	0.0988	989.3
333.15	0.1980	995.4
333.15	0.3312	1002.7
333.15	0.5005	1010.0
333.15	0.6720	1013.0
333.15	0.8044	1012.2
333.15	0.9481	1007.8
333.15	1.0000	1005.3
343.15	0.0000	978.6
343.15	0.0988	983.5
343.15	0.1980	989.2
343.15	0.3312	996.0
343.15	0.5005	1002.3
343.15	0.6720	1004.9
343.15	0.8044	1004.1
343.15	0.9481	999.8
343.15	1.0000	997.7
353.15	0.0000	972.7
353.15	0.0988	977.2
353.15	0.1980	982.5
353.15	0.3312	988.9
353.15	0.5005	994.6
353.15	0.6720	996.9
353.15	0.8044	996.0
353.15	0.9481	991.9
353.15	1.0000	989.5
253.15	0.5005	1062.5
253.15	0.6720	1070.8
253.15	0.8044	1071.6
253.15	0.9481	1068.2
253.15	1.0000	1065.8
258.15	0.3312	1041.7
258.15	0.5005	1059.8
258.15	0.6720	1067.6
258.15	0.8044	1068.1
258.15	0.9481	1064.7
258.15	1.0000	1062.2
263.15	0.3312	1040.0
263.15	0.5005	1056.9
263.15	0.6720	1064.3
263.15	0.8044	1064.5
263.15	0.9481	1061.0
263.15	1.0000	1058.6
268.15	0.1980	1021.7
268.15	0.3312	1038.15
268.15	0.5005	1054.0
268.15	0.6720	1060.9
268.15	0.8044	1061.1
268.15	0.9481	1057.4
268.15	1.0000	1054.9

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0440	1033.39
298.15	0.0987	1034.15
298.15	0.1484	1034.84
298.15	0.2498	1036.3
298.15	0.3494	1037.8
298.15	0.4494	1039.24
298.15	0.5029	1039.87
298.15	0.5499	1040.27
298.15	0.5597	1040.33
298.15	0.6501	1040.2
298.15	0.7499	1037.73
298.15	0.8500	1030.31
298.15	0.9003	1023.26
298.15	0.9115	1021.26
298.15	0.9154	1020.51
298.15	0.9270	1018.16
298.15	0.9367	1016.02
298.15	0.9504	1012.69
298.15	0.9551	1011.46
298.15	0.9600	1010.13
298.15	0.9696	1007.36
298.15	0.9797	1004.21
298.15	0.9902	1000.65
298.15	0.9923	999.9
298.15	0.9948	998.99
308.15	0.0440	1026.01
308.15	0.0987	1026.76
308.15	0.1484	1027.45
308.15	0.2498	1028.92
308.15	0.3494	1030.43
308.15	0.4494	1031.91
308.15	0.5029	1032.59
308.15	0.5499	1033.05
308.15	0.5597	1033.12
308.15	0.6501	1033.19
308.15	0.7499	1031.14
308.15	0.8500	1024.53
308.15	0.9003	1018.14
308.15	0.9115	1016.3
308.15	0.9154	1015.63
308.15	0.9270	1013.47
308.15	0.9367	1011.51
308.15	0.9504	1008.45
308.15	0.9551	1007.32
308.15	0.9600	1006.1
308.15	0.9696	1003.55
308.15	0.9797	1000.65
308.15	0.9902	997.36
308.15	0.9923	996.67
308.15	0.9948	995.83
318.15	0.0440	1017.94
318.15	0.0987	1018.71
318.15	0.1484	1019.41
318.15	0.2498	1020.89
318.15	0.3494	1022.37
318.15	0.4494	1023.79
318.15	0.5029	1024.44
318.15	0.5499	1024.88
318.15	0.5597	1024.96
318.15	0.6501	1025.1
318.15	0.7499	1023.4
318.15	0.8500	1017.63
318.15	0.9003	1011.96
318.15	0.9115	1010.33
318.15	0.9154	1009.72
318.15	0.9270	1007.79
318.15	0.9367	1006.03
318.15	0.9504	1003.28
318.15	0.9551	1002.26
318.15	0.9600	1001.16
318.15	0.9696	998.86
318.15	0.9797	996.22
318.15	0.9902	993.24
318.15	0.9923	992.61
318.15	0.9948	991.85
328.15	0.0440	1010.15
328.15	0.0987	1010.89
328.15	0.1484	1011.57
328.15	0.2498	1012.99
328.15	0.3494	1014.43
328.15	0.4494	1015.82
328.15	0.5029	1016.47
328.15	0.5499	1016.94
328.15	0.5597	1017.01
328.15	0.6501	1017.26
328.15	0.7499	1015.84
328.15	0.8500	1010.71
328.15	0.9003	1005.57
328.15	0.9115	1004.09
328.15	0.9154	1003.54
328.15	0.9270	1001.78
328.15	0.9367	1000.17
328.15	0.9504	997.67
328.15	0.9551	996.73
328.15	0.9600	995.72
328.15	0.9696	993.62
328.15	0.9797	991.21
328.15	0.9902	988.47
328.15	0.9923	987.9
328.15	0.9948	987.19
338.15	0.0440	1002.38
338.15	0.0987	1003.08
338.15	0.1484	1003.72
338.15	0.2498	1005.08
338.15	0.3494	1006.46
338.15	0.4494	1007.81
338.15	0.5029	1008.45
338.15	0.5499	1008.91
338.15	0.5597	1008.99
338.15	0.6501	1009.3
338.15	0.7499	1008.09
338.15	0.8500	1003.47
338.15	0.9003	998.8
338.15	0.9115	997.45
338.15	0.9154	996.94
338.15	0.9270	995.33
338.15	0.9367	993.86
338.15	0.9504	991.56
338.15	0.9551	990.71
338.15	0.9600	989.78
338.15	0.9696	987.84
338.15	0.9797	985.63
338.15	0.9902	983.11
338.15	0.9923	982.58
338.15	0.9948	981.93

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Mole fraction of Propylene Glycol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.2500	296.65	1040.0
0.2500	313.05	1028.0
0.2500	333.10	1013.0
0.2500	353.05	996.5
0.2500	363.30	988.0
0.2500	373.45	979.3
0.2500	381.55	971.3
0.2500	390.55	963.4
0.2500	407.75	947.5
0.2500	424.55	930.2
0.2500	444.55	908.3
0.5000	297.05	1042.0
0.5000	313.05	1029.0
0.5000	333.10	1013.0
0.5000	353.05	996.8
0.5000	363.40	987.9
0.5000	383.50	970.3
0.5000	395.75	958.1
0.5000	407.45	947.1
0.5000	424.95	929.6
0.5000	439.95	914.7
0.7500	296.80	1038.0
0.7500	313.05	1026.0
0.7500	333.10	1010.0
0.7500	353.05	993.8
0.7500	363.35	985.1
0.7500	378.35	971.6
0.7500	388.50	963.2
0.7500	398.30	954.2
0.7500	408.15	944.7
0.7500	411.75	940.7
0.7500	428.15	924.7
0.7500	441.45	912.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propylene Glycol (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	997.05
298.15	0.0500	1011.79
298.15	0.1000	1022.73
298.15	0.1500	1030.33
298.15	0.2000	1035.27
298.15	0.2500	1038.27
298.15	0.3000	1039.85
298.15	0.3500	1040.55
298.15	0.4000	1040.6
298.15	0.4500	1040.28
298.15	0.5000	1039.83
298.15	0.5500	1039.24
298.15	0.6000	1038.53
298.15	0.6500	1037.84
298.15	0.7000	1037.09
298.15	0.7500	1036.33
298.15	0.8000	1035.57
298.15	0.8500	1034.81
298.15	0.9000	1034.08
298.15	0.9500	1033.35
298.15	1.0000	1032.69
308.15	0.0000	994.03
308.15	0.0500	1007.53
308.15	0.1000	1017.48
308.15	0.1500	1024.23
308.15	0.2000	1028.47
308.15	0.2500	1031.17
308.15	0.3000	1032.55
308.15	0.3500	1033.05
308.15	0.4000	1033.02
308.15	0.4500	1032.76
308.15	0.5000	1032.3
308.15	0.5500	1031.7
308.15	0.6000	1031.03
308.15	0.6500	1030.31
308.15	0.7000	1029.56
308.15	0.7500	1028.81
308.15	0.8000	1028.06
308.15	0.8500	1027.32
308.15	0.9000	1026.59
308.15	0.9500	1025.88
308.15	1.0000	1025.21
318.15	0.0000	990.16
318.15	0.0500	1002.61
318.15	0.1000	1011.69
318.15	0.1500	1017.73
318.15	0.2000	1021.65
318.15	0.2500	1023.85
318.15	0.3000	1025.01
318.15	0.3500	1025.42
318.15	0.4000	1025.34
318.15	0.4500	1025.05
318.15	0.5000	1024.54
318.15	0.5500	1023.93
318.15	0.6000	1023.29
318.15	0.6500	1022.58
318.15	0.7000	1021.87
318.15	0.7500	1021.11
318.15	0.8000	1020.37
318.15	0.8500	1019.61
318.15	0.9000	1018.9
318.15	0.9500	1018.19
318.15	1.0000	1017.51
328.15	0.0000	985.66
328.15	0.0500	997.16
328.15	0.1000	1005.39
328.15	0.1500	1010.88
328.15	0.2000	1014.32
328.15	0.2500	1016.27
328.15	0.3000	1017.25
328.15	0.3500	1017.54
328.15	0.4000	1017.47
328.15	0.4500	1017.1
328.15	0.5000	1016.59
328.15	0.5500	1016.0
328.15	0.6000	1015.39
328.15	0.6500	1014.69
328.15	0.7000	1014.0
328.15	0.7500	1013.3
328.15	0.8000	1012.54
328.15	0.8500	1011.8
328.15	0.9000	1011.06
328.15	0.9500	1010.37
328.15	1.0000	1009.78

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Molality, mol/kg of Water (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	1032.87
0.2187	1033.12
0.5592	1033.53
0.6141	1033.58
0.7341	1033.67
0.8421	1033.73
0.9215	1033.86
1.0234	1033.94

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Propylene Glycol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0731	1016.4
0.1555	1031.1
0.2449	1037.7
0.3384	1039.6
0.4321	1039.8
0.5223	1039.0
0.6058	1038.0
0.6803	1036.8
0.7446	1035.9
0.7987	1035.0
0.8430	1034.5
0.8786	1033.8
0.9068	1033.4
0.9355	1033.1

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 96.2 (Liquid)
• Mass fraction = 0.3 (Liquid)

Temperature, K - Liquid	Mass density, kg/m3 - Liquid
293.15	1023.1
303.15	1019.2
313.15	1014.5
323.15	1009.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mass fraction of Propylene Glycol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.2500	1020.98
293.15	0.2500	1019.08
298.15	0.2500	1017.01
303.15	0.2500	1014.78
308.15	0.2500	1012.38
313.15	0.2500	1009.84
318.15	0.2500	1007.15
288.15	0.5000	1041.16
293.15	0.5000	1038.02
298.15	0.5000	1034.79
303.15	0.5000	1031.49
308.15	0.5000	1028.11
313.15	0.5000	1024.66
318.15	0.5000	1021.13
288.15	0.7500	1047.67
293.15	0.7500	1044.04
298.15	0.7500	1040.37
303.15	0.7500	1036.64
308.15	0.7500	1032.88
313.15	0.7500	1029.06
318.15	0.7500	1025.19
288.15	0.2500	1020.99
293.15	0.2500	1019.1
298.15	0.2500	1017.02
303.15	0.2500	1014.79
308.15	0.2500	1012.39
313.15	0.2500	1009.85
293.15	0.2500	1019.09
298.15	0.7500	1040.36
308.15	0.7500	1032.87
313.15	0.7500	1029.05
293.15	0.5000	1038.01
298.15	0.5000	1034.78
303.15	0.5000	1031.48
313.15	0.5000	1024.65
318.15	0.5000	1021.12

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mass fraction of Propylene Glycol (1) - Liquid	Mass density, kg/m3 - Liquid
273.15	0.0000	1000.8
273.15	0.0988	1009.8
273.15	0.1980	1020.8
273.15	0.3312	1036.3
273.15	0.5005	1051.1
273.15	0.6720	1057.5
273.15	0.8044	1057.6
273.15	0.9481	1053.8
273.15	1.0000	1051.3
283.15	0.0000	1000.6
283.15	0.0988	1008.2
283.15	0.1980	1017.8
283.15	0.3312	1031.2
283.15	0.5005	1044.6
283.15	0.6720	1050.5
283.15	0.8044	1050.4
283.15	0.9481	1045.6
283.15	1.0000	1042.9
293.15	0.0000	999.3
293.15	0.0988	1005.7
293.15	0.1980	1014.5
293.15	0.3312	1026.3
293.15	0.5005	1038.1
293.15	0.6720	1043.2
293.15	0.8044	1042.9
293.15	0.9481	1038.2
293.15	1.0000	1035.5
303.15	0.0000	996.8
303.15	0.0988	1002.6
303.15	0.1980	1010.6
303.15	0.3312	1021.0
303.15	0.5005	1031.4
303.15	0.6720	1035.9
303.15	0.8044	1035.4
303.15	0.9481	1030.8
303.15	1.0000	1028.1
313.15	0.0000	993.2
313.15	0.0988	999.0
313.15	0.1980	1006.0
313.15	0.3312	1015.3
313.15	0.5005	1024.5
313.15	0.6720	1028.4
313.15	0.8044	1027.8
313.15	0.9481	1023.2
313.15	1.0000	1020.6
323.15	0.0000	989.0
323.15	0.0988	994.4
323.15	0.1980	1000.8
323.15	0.3312	1009.2
323.15	0.5005	1017.4
323.15	0.6720	1020.8
323.15	0.8044	1020.1
323.15	0.9481	1015.6
323.15	1.0000	1013.0
333.15	0.0000	984.4
333.15	0.0988	989.3
333.15	0.1980	995.4
333.15	0.3312	1002.7
333.15	0.5005	1010.0
333.15	0.6720	1013.0
333.15	0.8044	1012.2
333.15	0.9481	1007.8
333.15	1.0000	1005.3
343.15	0.0000	978.6
343.15	0.0988	983.5
343.15	0.1980	989.2
343.15	0.3312	996.0
343.15	0.5005	1002.3
343.15	0.6720	1004.9
343.15	0.8044	1004.1
343.15	0.9481	999.8
343.15	1.0000	997.7
353.15	0.0000	972.7
353.15	0.0988	977.2
353.15	0.1980	982.5
353.15	0.3312	988.9
353.15	0.5005	994.6
353.15	0.6720	996.9
353.15	0.8044	996.0
353.15	0.9481	991.9
353.15	1.0000	989.5
253.15	0.5005	1062.5
253.15	0.6720	1070.8
253.15	0.8044	1071.6
253.15	0.9481	1068.2
253.15	1.0000	1065.8
258.15	0.3312	1041.7
258.15	0.5005	1059.8
258.15	0.6720	1067.6
258.15	0.8044	1068.1
258.15	0.9481	1064.7
258.15	1.0000	1062.2
263.15	0.3312	1040.0
263.15	0.5005	1056.9
263.15	0.6720	1064.3
263.15	0.8044	1064.5
263.15	0.9481	1061.0
263.15	1.0000	1058.6
268.15	0.1980	1021.7
268.15	0.3312	1038.15
268.15	0.5005	1054.0
268.15	0.6720	1060.9
268.15	0.8044	1061.1
268.15	0.9481	1057.4
268.15	1.0000	1054.9

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0440	1033.39
298.15	0.0987	1034.15
298.15	0.1484	1034.84
298.15	0.2498	1036.3
298.15	0.3494	1037.8
298.15	0.4494	1039.24
298.15	0.5029	1039.87
298.15	0.5499	1040.27
298.15	0.5597	1040.33
298.15	0.6501	1040.2
298.15	0.7499	1037.73
298.15	0.8500	1030.31
298.15	0.9003	1023.26
298.15	0.9115	1021.26
298.15	0.9154	1020.51
298.15	0.9270	1018.16
298.15	0.9367	1016.02
298.15	0.9504	1012.69
298.15	0.9551	1011.46
298.15	0.9600	1010.13
298.15	0.9696	1007.36
298.15	0.9797	1004.21
298.15	0.9902	1000.65
298.15	0.9923	999.9
298.15	0.9948	998.99
308.15	0.0440	1026.01
308.15	0.0987	1026.76
308.15	0.1484	1027.45
308.15	0.2498	1028.92
308.15	0.3494	1030.43
308.15	0.4494	1031.91
308.15	0.5029	1032.59
308.15	0.5499	1033.05
308.15	0.5597	1033.12
308.15	0.6501	1033.19
308.15	0.7499	1031.14
308.15	0.8500	1024.53
308.15	0.9003	1018.14
308.15	0.9115	1016.3
308.15	0.9154	1015.63
308.15	0.9270	1013.47
308.15	0.9367	1011.51
308.15	0.9504	1008.45
308.15	0.9551	1007.32
308.15	0.9600	1006.1
308.15	0.9696	1003.55
308.15	0.9797	1000.65
308.15	0.9902	997.36
308.15	0.9923	996.67
308.15	0.9948	995.83
318.15	0.0440	1017.94
318.15	0.0987	1018.71
318.15	0.1484	1019.41
318.15	0.2498	1020.89
318.15	0.3494	1022.37
318.15	0.4494	1023.79
318.15	0.5029	1024.44
318.15	0.5499	1024.88
318.15	0.5597	1024.96
318.15	0.6501	1025.1
318.15	0.7499	1023.4
318.15	0.8500	1017.63
318.15	0.9003	1011.96
318.15	0.9115	1010.33
318.15	0.9154	1009.72
318.15	0.9270	1007.79
318.15	0.9367	1006.03
318.15	0.9504	1003.28
318.15	0.9551	1002.26
318.15	0.9600	1001.16
318.15	0.9696	998.86
318.15	0.9797	996.22
318.15	0.9902	993.24
318.15	0.9923	992.61
318.15	0.9948	991.85
328.15	0.0440	1010.15
328.15	0.0987	1010.89
328.15	0.1484	1011.57
328.15	0.2498	1012.99
328.15	0.3494	1014.43
328.15	0.4494	1015.82
328.15	0.5029	1016.47
328.15	0.5499	1016.94
328.15	0.5597	1017.01
328.15	0.6501	1017.26
328.15	0.7499	1015.84
328.15	0.8500	1010.71
328.15	0.9003	1005.57
328.15	0.9115	1004.09
328.15	0.9154	1003.54
328.15	0.9270	1001.78
328.15	0.9367	1000.17
328.15	0.9504	997.67
328.15	0.9551	996.73
328.15	0.9600	995.72
328.15	0.9696	993.62
328.15	0.9797	991.21
328.15	0.9902	988.47
328.15	0.9923	987.9
328.15	0.9948	987.19
338.15	0.0440	1002.38
338.15	0.0987	1003.08
338.15	0.1484	1003.72
338.15	0.2498	1005.08
338.15	0.3494	1006.46
338.15	0.4494	1007.81
338.15	0.5029	1008.45
338.15	0.5499	1008.91
338.15	0.5597	1008.99
338.15	0.6501	1009.3
338.15	0.7499	1008.09
338.15	0.8500	1003.47
338.15	0.9003	998.8
338.15	0.9115	997.45
338.15	0.9154	996.94
338.15	0.9270	995.33
338.15	0.9367	993.86
338.15	0.9504	991.56
338.15	0.9551	990.71
338.15	0.9600	989.78
338.15	0.9696	987.84
338.15	0.9797	985.63
338.15	0.9902	983.11
338.15	0.9923	982.58
338.15	0.9948	981.93

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Mole fraction of Propylene Glycol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.2500	296.65	1040.0
0.2500	313.05	1028.0
0.2500	333.10	1013.0
0.2500	353.05	996.5
0.2500	363.30	988.0
0.2500	373.45	979.3
0.2500	381.55	971.3
0.2500	390.55	963.4
0.2500	407.75	947.5
0.2500	424.55	930.2
0.2500	444.55	908.3
0.5000	297.05	1042.0
0.5000	313.05	1029.0
0.5000	333.10	1013.0
0.5000	353.05	996.8
0.5000	363.40	987.9
0.5000	383.50	970.3
0.5000	395.75	958.1
0.5000	407.45	947.1
0.5000	424.95	929.6
0.5000	439.95	914.7
0.7500	296.80	1038.0
0.7500	313.05	1026.0
0.7500	333.10	1010.0
0.7500	353.05	993.8
0.7500	363.35	985.1
0.7500	378.35	971.6
0.7500	388.50	963.2
0.7500	398.30	954.2
0.7500	408.15	944.7
0.7500	411.75	940.7
0.7500	428.15	924.7
0.7500	441.45	912.7

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Molality, mol/kg of Water (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1510.6
0.2187	1512.9
0.5592	1516.4
0.6141	1516.5
0.7341	1517.5
0.8421	1519.4
0.9215	1519.9
1.0234	1521.5

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mass fraction of Propylene Glycol (1) - Liquid	Speed of sound, m/s - Liquid
0.2500	1639.91
0.5000	1700.04
0.7500	1640.25

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0440	1511.4
298.15	0.0987	1518.3
298.15	0.1484	1523.0
298.15	0.2498	1531.6
298.15	0.3494	1551.3
298.15	0.4494	1581.6
298.15	0.5029	1602.9
298.15	0.5499	1622.2
298.15	0.5597	1626.9
298.15	0.6501	1660.5
298.15	0.7499	1687.6
298.15	0.8500	1676.8
298.15	0.9003	1642.7
298.15	0.9115	1632.5
298.15	0.9154	1627.5
298.15	0.9270	1614.3
298.15	0.9367	1602.1
298.15	0.9504	1582.9
298.15	0.9551	1577.5
298.15	0.9600	1570.2
298.15	0.9696	1554.1
298.15	0.9797	1535.9
298.15	0.9902	1518.0
298.15	0.9923	1513.6
298.15	0.9948	1508.4
308.15	0.0440	1502.9
308.15	0.0987	1509.5
308.15	0.1484	1513.1
308.15	0.2498	1524.5
308.15	0.3494	1541.8
308.15	0.4494	1565.2
308.15	0.5029	1581.4
308.15	0.5499	1598.4
308.15	0.5597	1602.2
308.15	0.6501	1640.0
308.15	0.7499	1672.3
308.15	0.8500	1660.9
308.15	0.9003	1628.3
308.15	0.9115	1618.4
308.15	0.9154	1614.8
308.15	0.9270	1603.4
308.15	0.9367	1593.2
308.15	0.9504	1578.0
308.15	0.9551	1572.6
308.15	0.9600	1566.9
308.15	0.9696	1555.5
308.15	0.9797	1543.3
308.15	0.9902	1530.7
308.15	0.9923	1528.2
308.15	0.9948	1525.2
318.15	0.0440	1451.7
318.15	0.0987	1458.8
318.15	0.1484	1463.2
318.15	0.2498	1476.1
318.15	0.3494	1495.1
318.15	0.4494	1520.3
318.15	0.5029	1537.6
318.15	0.5499	1555.5
318.15	0.5597	1559.6
318.15	0.6501	1599.9
318.15	0.7499	1637.6
318.15	0.8500	1637.9
318.15	0.9003	1615.0
318.15	0.9115	1607.7
318.15	0.9154	1605.0
318.15	0.9270	1596.5
318.15	0.9367	1589.0
318.15	0.9504	1577.7
318.15	0.9551	1573.6
318.15	0.9600	1569.4
318.15	0.9696	1561.0
318.15	0.9797	1552.2
318.15	0.9902	1543.1
318.15	0.9923	1541.4
318.15	0.9948	1539.3
328.15	0.0440	1414.3
328.15	0.0987	1421.8
328.15	0.1484	1426.6
328.15	0.2498	1440.5
328.15	0.3494	1460.2
328.15	0.4494	1486.4
328.15	0.5029	1504.2
328.15	0.5499	1522.6
328.15	0.5597	1526.7
328.15	0.6501	1568.3
328.15	0.7499	1609.2
328.15	0.8500	1617.9
328.15	0.9003	1602.5
328.15	0.9115	1597.2
328.15	0.9154	1595.2
328.15	0.9270	1589.0
328.15	0.9367	1583.4
328.15	0.9504	1575.1
328.15	0.9551	1572.2
328.15	0.9600	1569.1
328.15	0.9696	1563.1
328.15	0.9797	1556.8
328.15	0.9902	1550.5
328.15	0.9923	1549.3
328.15	0.9948	1547.8
338.15	0.0440	1395.8
338.15	0.0987	1403.2
338.15	0.1484	1408.2
338.15	0.2498	1422.2
338.15	0.3494	1441.9
338.15	0.4494	1468.0
338.15	0.5029	1485.6
338.15	0.5499	1503.8
338.15	0.5597	1507.9
338.15	0.6501	1549.0
338.15	0.7499	1590.8
338.15	0.8500	1604.3
338.15	0.9003	1593.6
338.15	0.9115	1589.7
338.15	0.9154	1588.2
338.15	0.9270	1583.5
338.15	0.9367	1579.2
338.15	0.9504	1572.9
338.15	0.9551	1570.7
338.15	0.9600	1568.4
338.15	0.9696	1563.8
338.15	0.9797	1559.2
338.15	0.9902	1554.7
338.15	0.9923	1553.9
338.15	0.9948	1552.9

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Molality, mol/kg of Water (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1510.6
0.2187	1512.9
0.5592	1516.4
0.6141	1516.5
0.7341	1517.5
0.8421	1519.4
0.9215	1519.9
1.0234	1521.5

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mass fraction of Propylene Glycol (1) - Liquid	Speed of sound, m/s - Liquid
0.2500	1639.91
0.5000	1700.04
0.7500	1640.25

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0440	1511.4
298.15	0.0987	1518.3
298.15	0.1484	1523.0
298.15	0.2498	1531.6
298.15	0.3494	1551.3
298.15	0.4494	1581.6
298.15	0.5029	1602.9
298.15	0.5499	1622.2
298.15	0.5597	1626.9
298.15	0.6501	1660.5
298.15	0.7499	1687.6
298.15	0.8500	1676.8
298.15	0.9003	1642.7
298.15	0.9115	1632.5
298.15	0.9154	1627.5
298.15	0.9270	1614.3
298.15	0.9367	1602.1
298.15	0.9504	1582.9
298.15	0.9551	1577.5
298.15	0.9600	1570.2
298.15	0.9696	1554.1
298.15	0.9797	1535.9
298.15	0.9902	1518.0
298.15	0.9923	1513.6
298.15	0.9948	1508.4
308.15	0.0440	1502.9
308.15	0.0987	1509.5
308.15	0.1484	1513.1
308.15	0.2498	1524.5
308.15	0.3494	1541.8
308.15	0.4494	1565.2
308.15	0.5029	1581.4
308.15	0.5499	1598.4
308.15	0.5597	1602.2
308.15	0.6501	1640.0
308.15	0.7499	1672.3
308.15	0.8500	1660.9
308.15	0.9003	1628.3
308.15	0.9115	1618.4
308.15	0.9154	1614.8
308.15	0.9270	1603.4
308.15	0.9367	1593.2
308.15	0.9504	1578.0
308.15	0.9551	1572.6
308.15	0.9600	1566.9
308.15	0.9696	1555.5
308.15	0.9797	1543.3
308.15	0.9902	1530.7
308.15	0.9923	1528.2
308.15	0.9948	1525.2
318.15	0.0440	1451.7
318.15	0.0987	1458.8
318.15	0.1484	1463.2
318.15	0.2498	1476.1
318.15	0.3494	1495.1
318.15	0.4494	1520.3
318.15	0.5029	1537.6
318.15	0.5499	1555.5
318.15	0.5597	1559.6
318.15	0.6501	1599.9
318.15	0.7499	1637.6
318.15	0.8500	1637.9
318.15	0.9003	1615.0
318.15	0.9115	1607.7
318.15	0.9154	1605.0
318.15	0.9270	1596.5
318.15	0.9367	1589.0
318.15	0.9504	1577.7
318.15	0.9551	1573.6
318.15	0.9600	1569.4
318.15	0.9696	1561.0
318.15	0.9797	1552.2
318.15	0.9902	1543.1
318.15	0.9923	1541.4
318.15	0.9948	1539.3
328.15	0.0440	1414.3
328.15	0.0987	1421.8
328.15	0.1484	1426.6
328.15	0.2498	1440.5
328.15	0.3494	1460.2
328.15	0.4494	1486.4
328.15	0.5029	1504.2
328.15	0.5499	1522.6
328.15	0.5597	1526.7
328.15	0.6501	1568.3
328.15	0.7499	1609.2
328.15	0.8500	1617.9
328.15	0.9003	1602.5
328.15	0.9115	1597.2
328.15	0.9154	1595.2
328.15	0.9270	1589.0
328.15	0.9367	1583.4
328.15	0.9504	1575.1
328.15	0.9551	1572.2
328.15	0.9600	1569.1
328.15	0.9696	1563.1
328.15	0.9797	1556.8
328.15	0.9902	1550.5
328.15	0.9923	1549.3
328.15	0.9948	1547.8
338.15	0.0440	1395.8
338.15	0.0987	1403.2
338.15	0.1484	1408.2
338.15	0.2498	1422.2
338.15	0.3494	1441.9
338.15	0.4494	1468.0
338.15	0.5029	1485.6
338.15	0.5499	1503.8
338.15	0.5597	1507.9
338.15	0.6501	1549.0
338.15	0.7499	1590.8
338.15	0.8500	1604.3
338.15	0.9003	1593.6
338.15	0.9115	1589.7
338.15	0.9154	1588.2
338.15	0.9270	1583.5
338.15	0.9367	1579.2
338.15	0.9504	1572.9
338.15	0.9551	1570.7
338.15	0.9600	1568.4
338.15	0.9696	1563.8
338.15	0.9797	1559.2
338.15	0.9902	1554.7
338.15	0.9923	1553.9
338.15	0.9948	1552.9

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propylene Glycol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
298.15	0.0000	0.0720
298.15	0.0500	0.0562
298.15	0.1000	0.0509
298.15	0.1500	0.0474
298.15	0.2000	0.0452
298.15	0.2500	0.0436
298.15	0.3000	0.0426
298.15	0.3500	0.0414
298.15	0.4000	0.0405
298.15	0.4500	0.0394
298.15	0.5000	0.0388
298.15	0.5500	0.0379
298.15	0.6000	0.0374
298.15	0.6500	0.0370
298.15	0.7000	0.0368
298.15	0.7500	0.0366
298.15	0.8000	0.0364
298.15	0.8500	0.0363
298.15	0.9000	0.0361
298.15	0.9500	0.0359
298.15	1.0000	0.0357
308.15	0.0000	0.0703
308.15	0.0500	0.0549
308.15	0.1000	0.0499
308.15	0.1500	0.0465
308.15	0.2000	0.0444
308.15	0.2500	0.0429
308.15	0.3000	0.0419
308.15	0.3500	0.0409
308.15	0.4000	0.0398
308.15	0.4500	0.0389
308.15	0.5000	0.0383
308.15	0.5500	0.0375
308.15	0.6000	0.0369
308.15	0.6500	0.0366
308.15	0.7000	0.0364
308.15	0.7500	0.0362
308.15	0.8000	0.0361
308.15	0.8500	0.0359
308.15	0.9000	0.0358
308.15	0.9500	0.0355
308.15	1.0000	0.0353
318.15	0.0000	0.0687
318.15	0.0500	0.0539
318.15	0.1000	0.0489
318.15	0.1500	0.0457
318.15	0.2000	0.0435
318.15	0.2500	0.0421
318.15	0.3000	0.0412
318.15	0.3500	0.0402
318.15	0.4000	0.0392
318.15	0.4500	0.0384
318.15	0.5000	0.0377
318.15	0.5500	0.0371
318.15	0.6000	0.0366
318.15	0.6500	0.0362
318.15	0.7000	0.0359
318.15	0.7500	0.0358
318.15	0.8000	0.0357
318.15	0.8500	0.0355
318.15	0.9000	0.0354
318.15	0.9500	0.0351
318.15	1.0000	0.0350
328.15	0.0000	0.0669
328.15	0.0500	0.0526
328.15	0.1000	0.0478
328.15	0.1500	0.0447
328.15	0.2000	0.0425
328.15	0.2500	0.0412
328.15	0.3000	0.0404
328.15	0.3500	0.0395
328.15	0.4000	0.0386
328.15	0.4500	0.0378
328.15	0.5000	0.0372
328.15	0.5500	0.0365
328.15	0.6000	0.0362
328.15	0.6500	0.0357
328.15	0.7000	0.0355
328.15	0.7500	0.0353
328.15	0.8000	0.0352
328.15	0.8500	0.0350
328.15	0.9000	0.0349
328.15	0.9500	0.0348
328.15	1.0000	0.0346

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propylene Glycol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
298.15	0.0000	0.0720
298.15	0.0500	0.0562
298.15	0.1000	0.0509
298.15	0.1500	0.0474
298.15	0.2000	0.0452
298.15	0.2500	0.0436
298.15	0.3000	0.0426
298.15	0.3500	0.0414
298.15	0.4000	0.0405
298.15	0.4500	0.0394
298.15	0.5000	0.0388
298.15	0.5500	0.0379
298.15	0.6000	0.0374
298.15	0.6500	0.0370
298.15	0.7000	0.0368
298.15	0.7500	0.0366
298.15	0.8000	0.0364
298.15	0.8500	0.0363
298.15	0.9000	0.0361
298.15	0.9500	0.0359
298.15	1.0000	0.0357
308.15	0.0000	0.0703
308.15	0.0500	0.0549
308.15	0.1000	0.0499
308.15	0.1500	0.0465
308.15	0.2000	0.0444
308.15	0.2500	0.0429
308.15	0.3000	0.0419
308.15	0.3500	0.0409
308.15	0.4000	0.0398
308.15	0.4500	0.0389
308.15	0.5000	0.0383
308.15	0.5500	0.0375
308.15	0.6000	0.0369
308.15	0.6500	0.0366
308.15	0.7000	0.0364
308.15	0.7500	0.0362
308.15	0.8000	0.0361
308.15	0.8500	0.0359
308.15	0.9000	0.0358
308.15	0.9500	0.0355
308.15	1.0000	0.0353
318.15	0.0000	0.0687
318.15	0.0500	0.0539
318.15	0.1000	0.0489
318.15	0.1500	0.0457
318.15	0.2000	0.0435
318.15	0.2500	0.0421
318.15	0.3000	0.0412
318.15	0.3500	0.0402
318.15	0.4000	0.0392
318.15	0.4500	0.0384
318.15	0.5000	0.0377
318.15	0.5500	0.0371
318.15	0.6000	0.0366
318.15	0.6500	0.0362
318.15	0.7000	0.0359
318.15	0.7500	0.0358
318.15	0.8000	0.0357
318.15	0.8500	0.0355
318.15	0.9000	0.0354
318.15	0.9500	0.0351
318.15	1.0000	0.0350
328.15	0.0000	0.0669
328.15	0.0500	0.0526
328.15	0.1000	0.0478
328.15	0.1500	0.0447
328.15	0.2000	0.0425
328.15	0.2500	0.0412
328.15	0.3000	0.0404
328.15	0.3500	0.0395
328.15	0.4000	0.0386
328.15	0.4500	0.0378
328.15	0.5000	0.0372
328.15	0.5500	0.0365
328.15	0.6000	0.0362
328.15	0.6500	0.0357
328.15	0.7000	0.0355
328.15	0.7500	0.0353
328.15	0.8000	0.0352
328.15	0.8500	0.0350
328.15	0.9000	0.0349
328.15	0.9500	0.0348
328.15	1.0000	0.0346

Thermal conductivity, W/m/K [ref]

Operational conditions:

• Pressure, kPa = 96.2 (Liquid)
• Mass fraction = 0.3 (Liquid)

Temperature, K - Liquid	Thermal conductivity, W/m/K - Liquid
293.15	0.4430
303.15	0.4540
313.15	0.4630
323.15	0.4720

Thermal conductivity, W/m/K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Mole fraction of Propylene Glycol (1) - Liquid	Temperature, K - Liquid	Thermal conductivity, W/m/K - Liquid
0.2500	299.60	0.3220
0.2500	322.10	0.3370
0.2500	347.20	0.3480
0.2500	372.10	0.3530
0.2500	396.40	0.3530
0.2500	420.40	0.3470
0.2500	440.40	0.3380
0.5000	298.90	0.2430
0.5000	324.20	0.2500
0.5000	349.10	0.2540
0.5000	372.10	0.2550
0.5000	397.10	0.2550
0.5000	420.20	0.2530
0.5000	440.80	0.2490
0.7500	298.50	0.2120
0.7500	323.70	0.2140
0.7500	348.20	0.2150
0.7500	372.80	0.2150
0.7500	396.00	0.2140
0.7500	420.80	0.2120
0.7500	442.00	0.2100

Thermal conductivity, W/m/K [ref]

Operational conditions:

• Pressure, kPa = 96.2 (Liquid)
• Mass fraction = 0.3 (Liquid)

Temperature, K - Liquid	Thermal conductivity, W/m/K - Liquid
293.15	0.4430
303.15	0.4540
313.15	0.4630
323.15	0.4720

Thermal conductivity, W/m/K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Mole fraction of Propylene Glycol (1) - Liquid	Temperature, K - Liquid	Thermal conductivity, W/m/K - Liquid
0.2500	299.60	0.3220
0.2500	322.10	0.3370
0.2500	347.20	0.3480
0.2500	372.10	0.3530
0.2500	396.40	0.3530
0.2500	420.40	0.3470
0.2500	440.40	0.3380
0.5000	298.90	0.2430
0.5000	324.20	0.2500
0.5000	349.10	0.2540
0.5000	372.10	0.2550
0.5000	397.10	0.2550
0.5000	420.20	0.2530
0.5000	440.80	0.2490
0.7500	298.50	0.2120
0.7500	323.70	0.2140
0.7500	348.20	0.2150
0.7500	372.80	0.2150
0.7500	396.00	0.2140
0.7500	420.80	0.2120
0.7500	442.00	0.2100

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Molality, mol/kg of Propylene Glycol (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
1.0000	271.01
2.0	268.73
3.0	266.13
4.0	263.85
5.0	261.25

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Molality, mol/kg of Propylene Glycol (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
1.0000	271.01
2.0	268.73
3.0	266.13
4.0	263.85
5.0	261.25

Specific volume, m3/kg [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Volume fraction = 0.55 (Liquid)

Temperature, K - Liquid	Specific volume, m3/kg - Liquid
273.15	0.0009
274.15	0.0010
275.15	0.0010
276.15	0.0010
277.15	0.0010
278.15	0.0010
279.15	0.0010
280.15	0.0010
281.15	0.0010
282.15	0.0010
283.15	0.0010
284.15	0.0010
285.16	0.0010
286.16	0.0010
287.16	0.0010
288.16	0.0010
289.16	0.0010
290.16	0.0010
291.15	0.0010
292.15	0.0010
293.15	0.0010
294.15	0.0010
295.15	0.0010
296.16	0.0010
297.16	0.0010
298.16	0.0010
299.16	0.0010
300.16	0.0010
301.16	0.0010
302.16	0.0010
303.16	0.0010
304.16	0.0010
305.16	0.0010
306.16	0.0010
307.15	0.0010
308.15	0.0010
309.15	0.0010
310.15	0.0010
311.15	0.0010
312.15	0.0010
313.15	0.0010
288.13	0.0010
288.32	0.0010
288.13	0.0010

Specific volume, m3/kg [ref]

Operational condition: Volume fraction = 0.55 (Liquid)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Specific volume, m3/kg - Liquid
49500.00	288.03	0.0009
49600.00	288.12	0.0009
49800.00	288.33	0.0009
98100.00	288.13	0.0009
100100.00	288.00	0.0009
100900.00	288.30	0.0009
148600.00	288.13	0.0009
148900.00	288.04	0.0009
149300.00	288.31	0.0009
198700.00	288.12	0.0009
198800.00	287.99	0.0009
201100.00	288.31	0.0009
248600.00	288.11	0.0009
249300.00	288.22	0.0009
249400.00	288.33	0.0009
298400.00	288.11	0.0009
299200.00	288.36	0.0009
300500.00	288.31	0.0009
348400.00	288.12	0.0009
348700.00	288.31	0.0009
350000.00	288.35	0.0009

Specific volume, m3/kg [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Volume fraction = 0.55 (Liquid)

Temperature, K - Liquid	Specific volume, m3/kg - Liquid
273.15	0.0009
274.15	0.0010
275.15	0.0010
276.15	0.0010
277.15	0.0010
278.15	0.0010
279.15	0.0010
280.15	0.0010
281.15	0.0010
282.15	0.0010
283.15	0.0010
284.15	0.0010
285.16	0.0010
286.16	0.0010
287.16	0.0010
288.16	0.0010
289.16	0.0010
290.16	0.0010
291.15	0.0010
292.15	0.0010
293.15	0.0010
294.15	0.0010
295.15	0.0010
296.16	0.0010
297.16	0.0010
298.16	0.0010
299.16	0.0010
300.16	0.0010
301.16	0.0010
302.16	0.0010
303.16	0.0010
304.16	0.0010
305.16	0.0010
306.16	0.0010
307.15	0.0010
308.15	0.0010
309.15	0.0010
310.15	0.0010
311.15	0.0010
312.15	0.0010
313.15	0.0010
288.13	0.0010
288.32	0.0010
288.13	0.0010

Specific volume, m3/kg [ref]

Operational condition: Volume fraction = 0.55 (Liquid)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Specific volume, m3/kg - Liquid
49500.00	288.03	0.0009
49600.00	288.12	0.0009
49800.00	288.33	0.0009
98100.00	288.13	0.0009
100100.00	288.00	0.0009
100900.00	288.30	0.0009
148600.00	288.13	0.0009
148900.00	288.04	0.0009
149300.00	288.31	0.0009
198700.00	288.12	0.0009
198800.00	287.99	0.0009
201100.00	288.31	0.0009
248600.00	288.11	0.0009
249300.00	288.22	0.0009
249400.00	288.33	0.0009
298400.00	288.11	0.0009
299200.00	288.36	0.0009
300500.00	288.31	0.0009
348400.00	288.12	0.0009
348700.00	288.31	0.0009
350000.00	288.35	0.0009

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propylene Glycol (1) - Liquid	Excess molar volume, m3/mol - Liquid
283.15	0.0222	-6.4900e-08
283.15	0.0562	-1.9510e-07
283.15	0.0784	-2.9020e-07
283.15	0.1224	-4.5080e-07
283.15	0.1545	-5.5200e-07
283.15	0.1667	-5.8300e-07
283.15	0.1873	-6.2770e-07
283.15	0.1918	-6.2740e-07
283.15	0.2272	-6.9300e-07
283.15	0.2878	-7.4610e-07
283.15	0.3965	-7.4610e-07
283.15	0.4863	-7.0250e-07
283.15	0.5274	-6.7270e-07
283.15	0.6388	-5.5030e-07
283.15	0.7530	-3.9800e-07
283.15	0.7757	-3.7020e-07
283.15	0.8592	-2.4150e-07
283.15	0.9045	-1.7060e-07
283.15	0.9069	-1.5850e-07
283.15	0.9677	-5.6400e-08
293.15	0.0222	-6.3400e-08
293.15	0.0562	-1.8520e-07
293.15	0.0784	-2.7210e-07
293.15	0.1224	-4.1730e-07
293.15	0.1545	-5.0940e-07
293.15	0.1667	-5.3770e-07
293.15	0.1873	-5.7900e-07
293.15	0.1918	-5.7820e-07
293.15	0.2272	-6.4000e-07
293.15	0.2878	-6.9120e-07
293.15	0.3965	-6.9450e-07
293.15	0.4863	-6.5640e-07
293.15	0.5274	-6.3010e-07
293.15	0.6388	-5.1700e-07
293.15	0.7530	-3.7480e-07
293.15	0.7757	-3.4940e-07
293.15	0.8592	-2.2830e-07
293.15	0.9045	-1.6200e-07
293.15	0.9069	-1.4980e-07
293.15	0.9677	-5.3900e-08
298.15	0.0222	-6.2800e-08
298.15	0.0562	-1.8120e-07
298.15	0.0784	-2.6480e-07
298.15	0.1224	-4.0320e-07
298.15	0.1545	-4.9130e-07
298.15	0.1667	-5.1850e-07
298.15	0.1873	-5.5820e-07
298.15	0.1918	-5.5710e-07
298.15	0.2272	-6.1710e-07
298.15	0.2878	-6.6740e-07
298.15	0.3965	-6.7190e-07
298.15	0.4863	-6.3610e-07
298.15	0.5274	-6.1140e-07
298.15	0.6388	-5.0230e-07
298.15	0.7530	-3.6460e-07
298.15	0.7757	-3.4020e-07
298.15	0.8592	-2.2250e-07
298.15	0.9045	-1.5810e-07
298.15	0.9069	-1.4600e-07
298.15	0.9677	-5.2600e-08
303.15	0.0222	-6.2100e-08
303.15	0.0562	-1.7760e-07
303.15	0.0784	-2.5810e-07
303.15	0.1224	-3.9050e-07
303.15	0.1545	-4.7500e-07
303.15	0.1667	-5.0110e-07
303.15	0.1873	-5.3920e-07
303.15	0.1918	-5.3790e-07
303.15	0.2272	-5.9620e-07
303.15	0.2878	-6.4540e-07
303.15	0.3965	-6.5110e-07
303.15	0.4863	-6.1710e-07
303.15	0.5274	-5.9420e-07
303.15	0.6388	-4.8880e-07
303.15	0.7530	-3.5540e-07
303.15	0.7757	-3.3190e-07
303.15	0.8592	-2.1760e-07
303.15	0.9045	-1.5480e-07
303.15	0.9069	-1.4240e-07
303.15	0.9677	-5.1400e-08
313.15	0.0222	-6.0700e-08
313.15	0.0562	-1.7110e-07
313.15	0.0784	-2.4620e-07
313.15	0.1224	-3.6800e-07
313.15	0.1545	-4.4590e-07
313.15	0.1667	-4.7000e-07
313.15	0.1873	-5.0550e-07
313.15	0.1918	-5.0380e-07
313.15	0.2272	-5.5890e-07
313.15	0.2878	-6.0610e-07
313.15	0.3965	-6.1360e-07
313.15	0.4863	-5.8170e-07
313.15	0.5274	-5.6300e-07
313.15	0.6388	-4.6460e-07
313.15	0.7530	-3.3890e-07
313.15	0.7757	-3.1710e-07
313.15	0.8592	-2.0840e-07
313.15	0.9045	-1.4870e-07
313.15	0.9069	-1.3640e-07
313.15	0.9677	-4.9400e-08

Partial molar volume, m3/mol of Propylene Glycol (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Partial molar volume, m3/mol of Propylene Glycol (1) - Liquid
298.21	640.00	0.0001
298.22	15160.00	0.0001
298.22	29790.00	0.0001
318.17	500.00	0.0001
318.17	14770.00	0.0001
318.17	30140.00	0.0001
338.16	440.00	0.0001
338.16	15160.00	0.0001
338.16	30320.00	0.0001
373.13	15150.00	0.0001
373.13	29980.00	0.0001
373.14	2010.00	0.0001
408.15	29980.00	0.0001
408.16	1760.00	0.0001
408.16	15000.00	0.0001
441.99	1840.00	0.0001
442.03	15650.00	0.0001
442.03	29800.00	0.0001
473.15	1890.00	0.0001
473.15	15760.00	0.0001
473.16	30230.00	0.0001
498.15	2930.00	0.0001
498.15	15970.00	0.0001
498.15	30110.00	0.0001
523.16	4980.00	0.0001
523.16	16130.00	0.0001
523.16	30320.00	0.0001
548.17	7020.00	0.0001
548.18	18020.00	0.0001
548.18	30440.00	0.0001
573.14	30360.00	0.0001
573.18	10120.00	0.0001
573.19	19990.00	0.0001

Excess molar volume, m3/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Propylene Glycol (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0731	-2.1920e-07
0.1555	-4.7980e-07
0.2449	-6.2020e-07
0.3384	-6.6180e-07
0.4321	-6.5250e-07
0.5223	-5.9850e-07
0.6058	-5.3110e-07
0.6803	-4.4930e-07
0.7446	-3.7310e-07
0.7987	-3.0050e-07
0.8430	-2.4770e-07
0.8786	-1.8910e-07
0.9068	-1.4590e-07
0.9355	-1.0520e-07

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Propylene Glycol (1) - Liquid	Excess molar volume, m3/mol - Liquid
283.15	0.0222	-6.4900e-08
283.15	0.0562	-1.9510e-07
283.15	0.0784	-2.9020e-07
283.15	0.1224	-4.5080e-07
283.15	0.1545	-5.5200e-07
283.15	0.1667	-5.8300e-07
283.15	0.1873	-6.2770e-07
283.15	0.1918	-6.2740e-07
283.15	0.2272	-6.9300e-07
283.15	0.2878	-7.4610e-07
283.15	0.3965	-7.4610e-07
283.15	0.4863	-7.0250e-07
283.15	0.5274	-6.7270e-07
283.15	0.6388	-5.5030e-07
283.15	0.7530	-3.9800e-07
283.15	0.7757	-3.7020e-07
283.15	0.8592	-2.4150e-07
283.15	0.9045	-1.7060e-07
283.15	0.9069	-1.5850e-07
283.15	0.9677	-5.6400e-08
293.15	0.0222	-6.3400e-08
293.15	0.0562	-1.8520e-07
293.15	0.0784	-2.7210e-07
293.15	0.1224	-4.1730e-07
293.15	0.1545	-5.0940e-07
293.15	0.1667	-5.3770e-07
293.15	0.1873	-5.7900e-07
293.15	0.1918	-5.7820e-07
293.15	0.2272	-6.4000e-07
293.15	0.2878	-6.9120e-07
293.15	0.3965	-6.9450e-07
293.15	0.4863	-6.5640e-07
293.15	0.5274	-6.3010e-07
293.15	0.6388	-5.1700e-07
293.15	0.7530	-3.7480e-07
293.15	0.7757	-3.4940e-07
293.15	0.8592	-2.2830e-07
293.15	0.9045	-1.6200e-07
293.15	0.9069	-1.4980e-07
293.15	0.9677	-5.3900e-08
298.15	0.0222	-6.2800e-08
298.15	0.0562	-1.8120e-07
298.15	0.0784	-2.6480e-07
298.15	0.1224	-4.0320e-07
298.15	0.1545	-4.9130e-07
298.15	0.1667	-5.1850e-07
298.15	0.1873	-5.5820e-07
298.15	0.1918	-5.5710e-07
298.15	0.2272	-6.1710e-07
298.15	0.2878	-6.6740e-07
298.15	0.3965	-6.7190e-07
298.15	0.4863	-6.3610e-07
298.15	0.5274	-6.1140e-07
298.15	0.6388	-5.0230e-07
298.15	0.7530	-3.6460e-07
298.15	0.7757	-3.4020e-07
298.15	0.8592	-2.2250e-07
298.15	0.9045	-1.5810e-07
298.15	0.9069	-1.4600e-07
298.15	0.9677	-5.2600e-08
303.15	0.0222	-6.2100e-08
303.15	0.0562	-1.7760e-07
303.15	0.0784	-2.5810e-07
303.15	0.1224	-3.9050e-07
303.15	0.1545	-4.7500e-07
303.15	0.1667	-5.0110e-07
303.15	0.1873	-5.3920e-07
303.15	0.1918	-5.3790e-07
303.15	0.2272	-5.9620e-07
303.15	0.2878	-6.4540e-07
303.15	0.3965	-6.5110e-07
303.15	0.4863	-6.1710e-07
303.15	0.5274	-5.9420e-07
303.15	0.6388	-4.8880e-07
303.15	0.7530	-3.5540e-07
303.15	0.7757	-3.3190e-07
303.15	0.8592	-2.1760e-07
303.15	0.9045	-1.5480e-07
303.15	0.9069	-1.4240e-07
303.15	0.9677	-5.1400e-08
313.15	0.0222	-6.0700e-08
313.15	0.0562	-1.7110e-07
313.15	0.0784	-2.4620e-07
313.15	0.1224	-3.6800e-07
313.15	0.1545	-4.4590e-07
313.15	0.1667	-4.7000e-07
313.15	0.1873	-5.0550e-07
313.15	0.1918	-5.0380e-07
313.15	0.2272	-5.5890e-07
313.15	0.2878	-6.0610e-07
313.15	0.3965	-6.1360e-07
313.15	0.4863	-5.8170e-07
313.15	0.5274	-5.6300e-07
313.15	0.6388	-4.6460e-07
313.15	0.7530	-3.3890e-07
313.15	0.7757	-3.1710e-07
313.15	0.8592	-2.0840e-07
313.15	0.9045	-1.4870e-07
313.15	0.9069	-1.3640e-07
313.15	0.9677	-4.9400e-08

Partial molar volume, m3/mol of Propylene Glycol (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Partial molar volume, m3/mol of Propylene Glycol (1) - Liquid
298.21	640.00	0.0001
298.22	15160.00	0.0001
298.22	29790.00	0.0001
318.17	500.00	0.0001
318.17	14770.00	0.0001
318.17	30140.00	0.0001
338.16	440.00	0.0001
338.16	15160.00	0.0001
338.16	30320.00	0.0001
373.13	15150.00	0.0001
373.13	29980.00	0.0001
373.14	2010.00	0.0001
408.15	29980.00	0.0001
408.16	1760.00	0.0001
408.16	15000.00	0.0001
441.99	1840.00	0.0001
442.03	15650.00	0.0001
442.03	29800.00	0.0001
473.15	1890.00	0.0001
473.15	15760.00	0.0001
473.16	30230.00	0.0001
498.15	2930.00	0.0001
498.15	15970.00	0.0001
498.15	30110.00	0.0001
523.16	4980.00	0.0001
523.16	16130.00	0.0001
523.16	30320.00	0.0001
548.17	7020.00	0.0001
548.18	18020.00	0.0001
548.18	30440.00	0.0001
573.14	30360.00	0.0001
573.18	10120.00	0.0001
573.19	19990.00	0.0001

Excess molar volume, m3/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Propylene Glycol (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0731	-2.1920e-07
0.1555	-4.7980e-07
0.2449	-6.2020e-07
0.3384	-6.6180e-07
0.4321	-6.5250e-07
0.5223	-5.9850e-07
0.6058	-5.3110e-07
0.6803	-4.4930e-07
0.7446	-3.7310e-07
0.7987	-3.0050e-07
0.8430	-2.4770e-07
0.8786	-1.8910e-07
0.9068	-1.4590e-07
0.9355	-1.0520e-07

Sources

• Excess volumes and excess heat capacities for alkanediol + water systems in the temperature interval (283.15-313.15) K
• Densities, surface tensions, and isobaric vapor-liquid equilibria for the mixtures of 2-propanol, water, and 1,2-propanediol
• Measurement and correlation of excess molar enthalpy for(1,2-propanediol, or 1,3-propanediol, or 1,4-butanediol + water) at the temperatures (298.15, 323.15, and 343.15) K
• Partial molar volumes of organic solutes in water. XIV. Polyhydric alcohols derived from ethane and propane at temperatures T = 298 K to T = 573 K and at pressures up to 30 MPa
• Volumetric and compressibility properties of liquid water as a solute in glycolic, propylene carbonate, and tetramethylurea solutions at T = 298.15 K
• Experimental study of the excess molar volume of ternary mixtures containing {water + (1,2-propanediol, or 1,3-propanediol, or 1,2-butanediol, or 1,3-butanediol, or 1,4-butanediol, or 2,3-butanediol) + electrolytes} at a temperature of 298.15 K and atmospheric pressure
• Potential heat transfer enhancement of functionalized graphene nanoplatelet dispersions in a propylene glycol-water mixture. Thermophysical profile
• Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
• DSC determination of partial ternary phase diagrams of methanol/sodium chloride/water and propylene glycol/sodium chloride/water and their applications for synthesized diagrams
• Apparent Molar Volumes and Isentropic Compressibilities of Tetraalkylammonium Bromides in Aqueous Propane-1,2-diol. An Attempt to Design Hydraulic Liquids
• Viscosities, Densities, and Refractive Indices of Aqueous Propane-1,3-diol
• Densities, Dynamic Viscosities, Speeds of Sound, and Relative Permittivities for Water + Alkanediols (Propane-1,2- and -1,3-diol and Butane-1,2-, -1,3-, -1,4-, and -2,3-Diol) at Different Temperatures
• Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K
• Vapor Liquid Equilibria for Water + Propylene Glycols Binary Systems: Experimental Data and Regression
• Volumetric Properties of Pressure-Transmitting Fluids up to 350 MPa: Water, Ethanol, Ethylene Glycol, Propylene Glycol, Castor Oil, Silicon Oil, and Some of Their Binary Mixture