Datasets
-
Mole fraction (2)
-
η - Viscosity, Pa*s (4)
-
Excess molar heat capacity, J/K/mol (6)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
n0 - Refractive index (Na D-line) (2)
-
ρl - Mass density, kg/m3 (8)
-
csound,fluid - Speed of Sound, m/s (4)
-
Tboil - Boiling temperature at pressure P, K (2)
-
Excess molar volume, m3/mol (6)
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Water (2) - Liquid |
Mole fraction of Water (2) - Gas |
0.0780 |
0.7640 |
0.1750 |
0.9180 |
0.2470 |
0.9530 |
0.3410 |
0.9740 |
0.4020 |
0.9810 |
0.4590 |
0.9850 |
0.5270 |
0.9890 |
0.5710 |
0.9910 |
0.6330 |
0.9930 |
0.6820 |
0.9940 |
0.7330 |
0.9950 |
0.7780 |
1.0000 |
0.8210 |
1.0000 |
0.8800 |
1.0000 |
0.9320 |
1.0000 |
0.9800 |
1.0000 |
1.0000 |
1.0000 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Water (2) - Liquid |
Mole fraction of Water (2) - Gas |
0.0780 |
0.7640 |
0.1750 |
0.9180 |
0.2470 |
0.9530 |
0.3410 |
0.9740 |
0.4020 |
0.9810 |
0.4590 |
0.9850 |
0.5270 |
0.9890 |
0.5710 |
0.9910 |
0.6330 |
0.9930 |
0.6820 |
0.9940 |
0.7330 |
0.9950 |
0.7780 |
1.0000 |
0.8210 |
1.0000 |
0.8800 |
1.0000 |
0.9320 |
1.0000 |
0.9800 |
1.0000 |
1.0000 |
1.0000 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of 1,3-Propanediol (1) - Liquid |
Viscosity, Pa*s - Liquid |
273.15 |
0.0000 |
0.0018 |
273.15 |
0.1113 |
0.0029 |
273.15 |
0.2226 |
0.0047 |
273.15 |
0.3340 |
0.0073 |
273.15 |
0.4453 |
0.0117 |
273.15 |
0.5010 |
0.0145 |
273.15 |
0.6123 |
0.0249 |
273.15 |
0.7236 |
0.0416 |
273.15 |
0.8349 |
0.0707 |
273.15 |
0.9277 |
0.1097 |
273.15 |
1.0000 |
0.1527 |
283.15 |
0.0000 |
0.0013 |
283.15 |
0.1113 |
0.0021 |
283.15 |
0.2226 |
0.0032 |
283.15 |
0.3340 |
0.0047 |
283.15 |
0.4453 |
0.0075 |
283.15 |
0.5010 |
0.0091 |
283.15 |
0.6123 |
0.0151 |
283.15 |
0.7236 |
0.0246 |
283.15 |
0.8349 |
0.0408 |
283.15 |
0.9277 |
0.0623 |
283.15 |
1.0000 |
0.0865 |
293.15 |
0.0000 |
0.0010 |
293.15 |
0.1113 |
0.0015 |
293.15 |
0.2226 |
0.0023 |
293.15 |
0.3340 |
0.0033 |
293.15 |
0.4453 |
0.0050 |
293.15 |
0.5010 |
0.0061 |
293.15 |
0.6123 |
0.0098 |
293.15 |
0.7236 |
0.0155 |
293.15 |
0.8349 |
0.0250 |
293.15 |
0.9277 |
0.0376 |
293.15 |
1.0000 |
0.0520 |
303.15 |
0.0000 |
0.0008 |
303.15 |
0.1113 |
0.0012 |
303.15 |
0.2226 |
0.0017 |
303.15 |
0.3340 |
0.0024 |
303.15 |
0.4453 |
0.0036 |
303.15 |
0.5010 |
0.0043 |
303.15 |
0.6123 |
0.0067 |
303.15 |
0.7236 |
0.0103 |
303.15 |
0.8349 |
0.0163 |
303.15 |
0.9277 |
0.0240 |
303.15 |
1.0000 |
0.0329 |
313.15 |
0.0000 |
0.0007 |
313.15 |
0.1113 |
0.0010 |
313.15 |
0.2226 |
0.0013 |
313.15 |
0.3340 |
0.0019 |
313.15 |
0.4453 |
0.0027 |
313.15 |
0.5010 |
0.0031 |
313.15 |
0.6123 |
0.0047 |
313.15 |
0.7236 |
0.0072 |
313.15 |
0.8349 |
0.0110 |
313.15 |
0.9277 |
0.0160 |
313.15 |
1.0000 |
0.0218 |
323.15 |
0.0000 |
0.0006 |
323.15 |
0.1113 |
0.0008 |
323.15 |
0.2226 |
0.0011 |
323.15 |
0.3340 |
0.0015 |
323.15 |
0.4453 |
0.0021 |
323.15 |
0.5010 |
0.0024 |
323.15 |
0.6123 |
0.0035 |
323.15 |
0.7236 |
0.0052 |
323.15 |
0.8349 |
0.0078 |
323.15 |
0.9277 |
0.0111 |
323.15 |
1.0000 |
0.0150 |
333.15 |
0.0000 |
0.0005 |
333.15 |
0.1113 |
0.0007 |
333.15 |
0.2226 |
0.0009 |
333.15 |
0.3340 |
0.0012 |
333.15 |
0.4453 |
0.0016 |
333.15 |
0.5010 |
0.0019 |
333.15 |
0.6123 |
0.0027 |
333.15 |
0.7236 |
0.0039 |
333.15 |
0.8349 |
0.0057 |
333.15 |
0.9277 |
0.0080 |
333.15 |
1.0000 |
0.0107 |
343.15 |
0.0000 |
0.0004 |
343.15 |
0.1113 |
0.0006 |
343.15 |
0.2226 |
0.0007 |
343.15 |
0.3340 |
0.0010 |
343.15 |
0.4453 |
0.0013 |
343.15 |
0.5010 |
0.0015 |
343.15 |
0.6123 |
0.0021 |
343.15 |
0.7236 |
0.0030 |
343.15 |
0.8349 |
0.0043 |
343.15 |
0.9277 |
0.0059 |
343.15 |
1.0000 |
0.0079 |
353.15 |
0.0000 |
0.0004 |
353.15 |
0.1113 |
0.0005 |
353.15 |
0.2226 |
0.0007 |
353.15 |
0.3340 |
0.0009 |
353.15 |
0.4453 |
0.0011 |
353.15 |
0.5010 |
0.0012 |
353.15 |
0.6123 |
0.0017 |
353.15 |
0.7236 |
0.0024 |
353.15 |
0.8349 |
0.0033 |
353.15 |
0.9277 |
0.0045 |
353.15 |
1.0000 |
0.0059 |
253.15 |
0.4453 |
0.0401 |
253.15 |
0.5010 |
0.0491 |
253.15 |
0.6123 |
0.0859 |
253.15 |
0.7236 |
0.1587 |
253.15 |
0.8349 |
0.2678 |
253.15 |
0.9277 |
0.4186 |
253.15 |
1.0000 |
0.5744 |
258.15 |
0.4453 |
0.0290 |
258.15 |
0.5010 |
0.0352 |
258.15 |
0.6123 |
0.0631 |
258.15 |
0.7236 |
0.1106 |
258.15 |
0.8349 |
0.1842 |
258.15 |
0.9277 |
0.2933 |
258.15 |
1.0000 |
0.4099 |
263.15 |
0.3340 |
0.0120 |
263.15 |
0.4453 |
0.0199 |
263.15 |
0.5010 |
0.0250 |
263.15 |
0.6123 |
0.0442 |
263.15 |
0.7236 |
0.0762 |
263.15 |
0.8349 |
0.1323 |
263.15 |
0.9277 |
0.2065 |
263.15 |
1.0000 |
0.2895 |
268.15 |
0.2226 |
0.0059 |
268.15 |
0.3340 |
0.0093 |
268.15 |
0.4453 |
0.0151 |
268.15 |
0.5010 |
0.0188 |
268.15 |
0.6123 |
0.0328 |
268.15 |
0.7236 |
0.0557 |
268.15 |
0.8349 |
0.0958 |
268.15 |
0.9277 |
0.1492 |
268.15 |
1.0000 |
0.2079 |
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 |
0.0622 |
0.0371 |
298.15 |
0.1496 |
0.0329 |
298.15 |
0.2563 |
0.0277 |
298.15 |
0.3500 |
0.0231 |
298.15 |
0.4555 |
0.0181 |
298.15 |
0.5000 |
0.0161 |
298.15 |
0.5548 |
0.0137 |
298.15 |
0.6522 |
0.0097 |
298.15 |
0.7553 |
0.0061 |
298.15 |
0.8522 |
0.0034 |
298.15 |
0.9085 |
0.0022 |
298.15 |
0.9147 |
0.0021 |
298.15 |
0.9255 |
0.0019 |
298.15 |
0.9350 |
0.0017 |
298.15 |
0.9548 |
0.0014 |
298.15 |
0.9556 |
0.0014 |
298.15 |
0.9602 |
0.0014 |
298.15 |
0.9700 |
0.0012 |
298.15 |
0.9801 |
0.0011 |
298.15 |
0.9897 |
0.0010 |
298.15 |
0.9921 |
0.0010 |
298.15 |
0.9951 |
0.0009 |
308.15 |
0.0622 |
0.0253 |
308.15 |
0.1496 |
0.0225 |
308.15 |
0.2563 |
0.0189 |
308.15 |
0.3500 |
0.0158 |
308.15 |
0.4555 |
0.0124 |
308.15 |
0.5000 |
0.0111 |
308.15 |
0.5548 |
0.0095 |
308.15 |
0.6522 |
0.0069 |
308.15 |
0.7553 |
0.0045 |
308.15 |
0.8522 |
0.0027 |
308.15 |
0.9085 |
0.0018 |
308.15 |
0.9147 |
0.0017 |
308.15 |
0.9255 |
0.0016 |
308.15 |
0.9350 |
0.0014 |
308.15 |
0.9548 |
0.0012 |
308.15 |
0.9556 |
0.0012 |
308.15 |
0.9602 |
0.0011 |
308.15 |
0.9700 |
0.0010 |
308.15 |
0.9801 |
0.0009 |
308.15 |
0.9897 |
0.0008 |
308.15 |
0.9921 |
0.0008 |
308.15 |
0.9951 |
0.0008 |
318.15 |
0.0622 |
0.0158 |
318.15 |
0.1496 |
0.0142 |
318.15 |
0.2563 |
0.0122 |
318.15 |
0.3500 |
0.0105 |
318.15 |
0.4555 |
0.0086 |
318.15 |
0.5000 |
0.0077 |
318.15 |
0.5548 |
0.0068 |
318.15 |
0.6522 |
0.0051 |
318.15 |
0.7553 |
0.0034 |
318.15 |
0.8522 |
0.0021 |
318.15 |
0.9085 |
0.0014 |
318.15 |
0.9147 |
0.0013 |
318.15 |
0.9255 |
0.0012 |
318.15 |
0.9350 |
0.0011 |
318.15 |
0.9548 |
0.0009 |
318.15 |
0.9556 |
0.0009 |
318.15 |
0.9602 |
0.0009 |
318.15 |
0.9700 |
0.0008 |
318.15 |
0.9801 |
0.0007 |
318.15 |
0.9897 |
0.0007 |
318.15 |
0.9921 |
0.0006 |
318.15 |
0.9951 |
0.0006 |
328.15 |
0.0622 |
0.0105 |
328.15 |
0.1496 |
0.0094 |
328.15 |
0.2563 |
0.0081 |
328.15 |
0.3500 |
0.0070 |
328.15 |
0.4555 |
0.0057 |
328.15 |
0.5000 |
0.0052 |
328.15 |
0.5548 |
0.0045 |
328.15 |
0.6522 |
0.0034 |
328.15 |
0.7553 |
0.0023 |
328.15 |
0.8522 |
0.0015 |
328.15 |
0.9085 |
0.0010 |
328.15 |
0.9147 |
0.0010 |
328.15 |
0.9255 |
0.0009 |
328.15 |
0.9350 |
0.0008 |
328.15 |
0.9548 |
0.0007 |
328.15 |
0.9556 |
0.0007 |
328.15 |
0.9602 |
0.0007 |
328.15 |
0.9700 |
0.0006 |
328.15 |
0.9801 |
0.0006 |
328.15 |
0.9897 |
0.0005 |
328.15 |
0.9921 |
0.0005 |
328.15 |
0.9951 |
0.0005 |
338.15 |
0.0622 |
0.0074 |
338.15 |
0.1496 |
0.0066 |
338.15 |
0.2563 |
0.0057 |
338.15 |
0.3500 |
0.0049 |
338.15 |
0.4555 |
0.0041 |
338.15 |
0.5000 |
0.0037 |
338.15 |
0.5548 |
0.0032 |
338.15 |
0.6522 |
0.0025 |
338.15 |
0.7553 |
0.0017 |
338.15 |
0.8522 |
0.0011 |
338.15 |
0.9085 |
0.0008 |
338.15 |
0.9147 |
0.0008 |
338.15 |
0.9255 |
0.0007 |
338.15 |
0.9350 |
0.0007 |
338.15 |
0.9548 |
0.0006 |
338.15 |
0.9556 |
0.0006 |
338.15 |
0.9602 |
0.0006 |
338.15 |
0.9700 |
0.0005 |
338.15 |
0.9801 |
0.0005 |
338.15 |
0.9897 |
0.0005 |
338.15 |
0.9921 |
0.0005 |
338.15 |
0.9951 |
0.0005 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of 1,3-Propanediol (1) - Liquid |
Viscosity, Pa*s - Liquid |
273.15 |
0.0000 |
0.0018 |
273.15 |
0.1113 |
0.0029 |
273.15 |
0.2226 |
0.0047 |
273.15 |
0.3340 |
0.0073 |
273.15 |
0.4453 |
0.0117 |
273.15 |
0.5010 |
0.0145 |
273.15 |
0.6123 |
0.0249 |
273.15 |
0.7236 |
0.0416 |
273.15 |
0.8349 |
0.0707 |
273.15 |
0.9277 |
0.1097 |
273.15 |
1.0000 |
0.1527 |
283.15 |
0.0000 |
0.0013 |
283.15 |
0.1113 |
0.0021 |
283.15 |
0.2226 |
0.0032 |
283.15 |
0.3340 |
0.0047 |
283.15 |
0.4453 |
0.0075 |
283.15 |
0.5010 |
0.0091 |
283.15 |
0.6123 |
0.0151 |
283.15 |
0.7236 |
0.0246 |
283.15 |
0.8349 |
0.0408 |
283.15 |
0.9277 |
0.0623 |
283.15 |
1.0000 |
0.0865 |
293.15 |
0.0000 |
0.0010 |
293.15 |
0.1113 |
0.0015 |
293.15 |
0.2226 |
0.0023 |
293.15 |
0.3340 |
0.0033 |
293.15 |
0.4453 |
0.0050 |
293.15 |
0.5010 |
0.0061 |
293.15 |
0.6123 |
0.0098 |
293.15 |
0.7236 |
0.0155 |
293.15 |
0.8349 |
0.0250 |
293.15 |
0.9277 |
0.0376 |
293.15 |
1.0000 |
0.0520 |
303.15 |
0.0000 |
0.0008 |
303.15 |
0.1113 |
0.0012 |
303.15 |
0.2226 |
0.0017 |
303.15 |
0.3340 |
0.0024 |
303.15 |
0.4453 |
0.0036 |
303.15 |
0.5010 |
0.0043 |
303.15 |
0.6123 |
0.0067 |
303.15 |
0.7236 |
0.0103 |
303.15 |
0.8349 |
0.0163 |
303.15 |
0.9277 |
0.0240 |
303.15 |
1.0000 |
0.0329 |
313.15 |
0.0000 |
0.0007 |
313.15 |
0.1113 |
0.0010 |
313.15 |
0.2226 |
0.0013 |
313.15 |
0.3340 |
0.0019 |
313.15 |
0.4453 |
0.0027 |
313.15 |
0.5010 |
0.0031 |
313.15 |
0.6123 |
0.0047 |
313.15 |
0.7236 |
0.0072 |
313.15 |
0.8349 |
0.0110 |
313.15 |
0.9277 |
0.0160 |
313.15 |
1.0000 |
0.0218 |
323.15 |
0.0000 |
0.0006 |
323.15 |
0.1113 |
0.0008 |
323.15 |
0.2226 |
0.0011 |
323.15 |
0.3340 |
0.0015 |
323.15 |
0.4453 |
0.0021 |
323.15 |
0.5010 |
0.0024 |
323.15 |
0.6123 |
0.0035 |
323.15 |
0.7236 |
0.0052 |
323.15 |
0.8349 |
0.0078 |
323.15 |
0.9277 |
0.0111 |
323.15 |
1.0000 |
0.0150 |
333.15 |
0.0000 |
0.0005 |
333.15 |
0.1113 |
0.0007 |
333.15 |
0.2226 |
0.0009 |
333.15 |
0.3340 |
0.0012 |
333.15 |
0.4453 |
0.0016 |
333.15 |
0.5010 |
0.0019 |
333.15 |
0.6123 |
0.0027 |
333.15 |
0.7236 |
0.0039 |
333.15 |
0.8349 |
0.0057 |
333.15 |
0.9277 |
0.0080 |
333.15 |
1.0000 |
0.0107 |
343.15 |
0.0000 |
0.0004 |
343.15 |
0.1113 |
0.0006 |
343.15 |
0.2226 |
0.0007 |
343.15 |
0.3340 |
0.0010 |
343.15 |
0.4453 |
0.0013 |
343.15 |
0.5010 |
0.0015 |
343.15 |
0.6123 |
0.0021 |
343.15 |
0.7236 |
0.0030 |
343.15 |
0.8349 |
0.0043 |
343.15 |
0.9277 |
0.0059 |
343.15 |
1.0000 |
0.0079 |
353.15 |
0.0000 |
0.0004 |
353.15 |
0.1113 |
0.0005 |
353.15 |
0.2226 |
0.0007 |
353.15 |
0.3340 |
0.0009 |
353.15 |
0.4453 |
0.0011 |
353.15 |
0.5010 |
0.0012 |
353.15 |
0.6123 |
0.0017 |
353.15 |
0.7236 |
0.0024 |
353.15 |
0.8349 |
0.0033 |
353.15 |
0.9277 |
0.0045 |
353.15 |
1.0000 |
0.0059 |
253.15 |
0.4453 |
0.0401 |
253.15 |
0.5010 |
0.0491 |
253.15 |
0.6123 |
0.0859 |
253.15 |
0.7236 |
0.1587 |
253.15 |
0.8349 |
0.2678 |
253.15 |
0.9277 |
0.4186 |
253.15 |
1.0000 |
0.5744 |
258.15 |
0.4453 |
0.0290 |
258.15 |
0.5010 |
0.0352 |
258.15 |
0.6123 |
0.0631 |
258.15 |
0.7236 |
0.1106 |
258.15 |
0.8349 |
0.1842 |
258.15 |
0.9277 |
0.2933 |
258.15 |
1.0000 |
0.4099 |
263.15 |
0.3340 |
0.0120 |
263.15 |
0.4453 |
0.0199 |
263.15 |
0.5010 |
0.0250 |
263.15 |
0.6123 |
0.0442 |
263.15 |
0.7236 |
0.0762 |
263.15 |
0.8349 |
0.1323 |
263.15 |
0.9277 |
0.2065 |
263.15 |
1.0000 |
0.2895 |
268.15 |
0.2226 |
0.0059 |
268.15 |
0.3340 |
0.0093 |
268.15 |
0.4453 |
0.0151 |
268.15 |
0.5010 |
0.0188 |
268.15 |
0.6123 |
0.0328 |
268.15 |
0.7236 |
0.0557 |
268.15 |
0.8349 |
0.0958 |
268.15 |
0.9277 |
0.1492 |
268.15 |
1.0000 |
0.2079 |
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 |
0.0622 |
0.0371 |
298.15 |
0.1496 |
0.0329 |
298.15 |
0.2563 |
0.0277 |
298.15 |
0.3500 |
0.0231 |
298.15 |
0.4555 |
0.0181 |
298.15 |
0.5000 |
0.0161 |
298.15 |
0.5548 |
0.0137 |
298.15 |
0.6522 |
0.0097 |
298.15 |
0.7553 |
0.0061 |
298.15 |
0.8522 |
0.0034 |
298.15 |
0.9085 |
0.0022 |
298.15 |
0.9147 |
0.0021 |
298.15 |
0.9255 |
0.0019 |
298.15 |
0.9350 |
0.0017 |
298.15 |
0.9548 |
0.0014 |
298.15 |
0.9556 |
0.0014 |
298.15 |
0.9602 |
0.0014 |
298.15 |
0.9700 |
0.0012 |
298.15 |
0.9801 |
0.0011 |
298.15 |
0.9897 |
0.0010 |
298.15 |
0.9921 |
0.0010 |
298.15 |
0.9951 |
0.0009 |
308.15 |
0.0622 |
0.0253 |
308.15 |
0.1496 |
0.0225 |
308.15 |
0.2563 |
0.0189 |
308.15 |
0.3500 |
0.0158 |
308.15 |
0.4555 |
0.0124 |
308.15 |
0.5000 |
0.0111 |
308.15 |
0.5548 |
0.0095 |
308.15 |
0.6522 |
0.0069 |
308.15 |
0.7553 |
0.0045 |
308.15 |
0.8522 |
0.0027 |
308.15 |
0.9085 |
0.0018 |
308.15 |
0.9147 |
0.0017 |
308.15 |
0.9255 |
0.0016 |
308.15 |
0.9350 |
0.0014 |
308.15 |
0.9548 |
0.0012 |
308.15 |
0.9556 |
0.0012 |
308.15 |
0.9602 |
0.0011 |
308.15 |
0.9700 |
0.0010 |
308.15 |
0.9801 |
0.0009 |
308.15 |
0.9897 |
0.0008 |
308.15 |
0.9921 |
0.0008 |
308.15 |
0.9951 |
0.0008 |
318.15 |
0.0622 |
0.0158 |
318.15 |
0.1496 |
0.0142 |
318.15 |
0.2563 |
0.0122 |
318.15 |
0.3500 |
0.0105 |
318.15 |
0.4555 |
0.0086 |
318.15 |
0.5000 |
0.0077 |
318.15 |
0.5548 |
0.0068 |
318.15 |
0.6522 |
0.0051 |
318.15 |
0.7553 |
0.0034 |
318.15 |
0.8522 |
0.0021 |
318.15 |
0.9085 |
0.0014 |
318.15 |
0.9147 |
0.0013 |
318.15 |
0.9255 |
0.0012 |
318.15 |
0.9350 |
0.0011 |
318.15 |
0.9548 |
0.0009 |
318.15 |
0.9556 |
0.0009 |
318.15 |
0.9602 |
0.0009 |
318.15 |
0.9700 |
0.0008 |
318.15 |
0.9801 |
0.0007 |
318.15 |
0.9897 |
0.0007 |
318.15 |
0.9921 |
0.0006 |
318.15 |
0.9951 |
0.0006 |
328.15 |
0.0622 |
0.0105 |
328.15 |
0.1496 |
0.0094 |
328.15 |
0.2563 |
0.0081 |
328.15 |
0.3500 |
0.0070 |
328.15 |
0.4555 |
0.0057 |
328.15 |
0.5000 |
0.0052 |
328.15 |
0.5548 |
0.0045 |
328.15 |
0.6522 |
0.0034 |
328.15 |
0.7553 |
0.0023 |
328.15 |
0.8522 |
0.0015 |
328.15 |
0.9085 |
0.0010 |
328.15 |
0.9147 |
0.0010 |
328.15 |
0.9255 |
0.0009 |
328.15 |
0.9350 |
0.0008 |
328.15 |
0.9548 |
0.0007 |
328.15 |
0.9556 |
0.0007 |
328.15 |
0.9602 |
0.0007 |
328.15 |
0.9700 |
0.0006 |
328.15 |
0.9801 |
0.0006 |
328.15 |
0.9897 |
0.0005 |
328.15 |
0.9921 |
0.0005 |
328.15 |
0.9951 |
0.0005 |
338.15 |
0.0622 |
0.0074 |
338.15 |
0.1496 |
0.0066 |
338.15 |
0.2563 |
0.0057 |
338.15 |
0.3500 |
0.0049 |
338.15 |
0.4555 |
0.0041 |
338.15 |
0.5000 |
0.0037 |
338.15 |
0.5548 |
0.0032 |
338.15 |
0.6522 |
0.0025 |
338.15 |
0.7553 |
0.0017 |
338.15 |
0.8522 |
0.0011 |
338.15 |
0.9085 |
0.0008 |
338.15 |
0.9147 |
0.0008 |
338.15 |
0.9255 |
0.0007 |
338.15 |
0.9350 |
0.0007 |
338.15 |
0.9548 |
0.0006 |
338.15 |
0.9556 |
0.0006 |
338.15 |
0.9602 |
0.0006 |
338.15 |
0.9700 |
0.0005 |
338.15 |
0.9801 |
0.0005 |
338.15 |
0.9897 |
0.0005 |
338.15 |
0.9921 |
0.0005 |
338.15 |
0.9951 |
0.0005 |
Excess molar heat capacity, J/K/mol
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,3-Propanediol (1) - Liquid |
Excess molar heat capacity, J/K/mol - Liquid |
283.15 |
0.0248 |
1.28 |
283.15 |
0.0369 |
1.89 |
283.15 |
0.0502 |
2.35 |
283.15 |
0.0751 |
2.54 |
283.15 |
0.1401 |
2.24 |
283.15 |
0.1504 |
2.2 |
283.15 |
0.2990 |
1.59 |
283.15 |
0.3982 |
1.31 |
283.15 |
0.4976 |
1.26 |
283.15 |
0.5955 |
1.15 |
283.15 |
0.7902 |
0.9800 |
283.15 |
0.9455 |
0.4800 |
293.15 |
0.0248 |
1.4 |
293.15 |
0.0369 |
2.08 |
293.15 |
0.0502 |
2.72 |
293.15 |
0.0751 |
3.22 |
293.15 |
0.1401 |
3.61 |
293.15 |
0.1504 |
3.67 |
293.15 |
0.2990 |
3.18 |
293.15 |
0.3982 |
2.66 |
293.15 |
0.4976 |
2.34 |
293.15 |
0.5955 |
1.92 |
293.15 |
0.7025 |
1.71 |
293.15 |
0.7902 |
1.19 |
293.15 |
0.9455 |
0.5300 |
298.15 |
0.0248 |
1.43 |
298.15 |
0.0369 |
2.13 |
298.15 |
0.0502 |
2.83 |
298.15 |
0.0751 |
3.44 |
298.15 |
0.1401 |
4.11 |
298.15 |
0.1504 |
4.21 |
298.15 |
0.2990 |
3.84 |
298.15 |
0.3982 |
3.28 |
298.15 |
0.4976 |
2.82 |
298.15 |
0.5955 |
2.33 |
298.15 |
0.7025 |
1.95 |
298.15 |
0.7902 |
1.3 |
298.15 |
0.9455 |
0.5800 |
303.15 |
0.0248 |
1.44 |
303.15 |
0.0369 |
2.16 |
303.15 |
0.0502 |
2.9 |
303.15 |
0.0751 |
3.59 |
303.15 |
0.1401 |
4.52 |
303.15 |
0.1504 |
4.64 |
303.15 |
0.2990 |
4.43 |
303.15 |
0.3982 |
3.85 |
303.15 |
0.4976 |
3.25 |
303.15 |
0.5955 |
2.74 |
303.15 |
0.7025 |
2.2 |
303.15 |
0.7902 |
1.4 |
303.15 |
0.9455 |
0.6100 |
313.15 |
0.0248 |
1.46 |
313.15 |
0.0369 |
2.26 |
313.15 |
0.0502 |
2.99 |
313.15 |
0.0751 |
3.8 |
313.15 |
0.1401 |
5.08 |
313.15 |
0.1504 |
5.27 |
313.15 |
0.2990 |
5.44 |
313.15 |
0.3982 |
4.81 |
313.15 |
0.4976 |
4.02 |
313.15 |
0.5955 |
3.48 |
313.15 |
0.7025 |
2.64 |
313.15 |
0.7902 |
1.49 |
313.15 |
0.9455 |
0.5500 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,3-Propanediol (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 |
0.0272 |
-0.2360 |
298.15 |
0.0591 |
-0.4530 |
298.15 |
0.1239 |
-0.7440 |
298.15 |
0.2087 |
-0.9240 |
298.15 |
0.3088 |
-1.011 |
298.15 |
0.3926 |
-1.034 |
298.15 |
0.5013 |
-0.9920 |
298.15 |
0.5510 |
-0.9040 |
298.15 |
0.6483 |
-0.7890 |
298.15 |
0.7430 |
-0.6330 |
298.15 |
0.8269 |
-0.4580 |
298.15 |
0.9249 |
-0.2560 |
323.15 |
0.0272 |
-0.1670 |
323.15 |
0.0591 |
-0.3200 |
323.15 |
0.1239 |
-0.5330 |
323.15 |
0.2087 |
-0.7300 |
323.15 |
0.3088 |
-0.8310 |
323.15 |
0.3926 |
-0.8320 |
323.15 |
0.5013 |
-0.8210 |
323.15 |
0.5510 |
-0.8130 |
323.15 |
0.6483 |
-0.7350 |
323.15 |
0.7430 |
-0.5840 |
323.15 |
0.8269 |
-0.4170 |
323.15 |
0.9249 |
-0.1950 |
343.15 |
0.0272 |
-0.1250 |
343.15 |
0.0591 |
-0.2290 |
343.15 |
0.1239 |
-0.3860 |
343.15 |
0.2087 |
-0.4640 |
343.15 |
0.3088 |
-0.5600 |
343.15 |
0.3926 |
-0.5910 |
343.15 |
0.5013 |
-0.5930 |
343.15 |
0.5510 |
-0.5790 |
343.15 |
0.6483 |
-0.5050 |
343.15 |
0.7430 |
-0.4330 |
343.15 |
0.8269 |
-0.3080 |
343.15 |
0.9249 |
-0.1530 |
Molar enthalpy of dilution, kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Fixed |
Measured |
Initial molality of solute, mol/kg - Liquid |
Final molality of solute, mol/kg - Liquid |
Molar enthalpy of dilution, kJ/mol - Liquid |
0.0012 |
0.0052 |
-0.2008 |
0.0052 |
0.0092 |
-0.1978 |
0.0092 |
0.0131 |
-0.1936 |
0.0131 |
0.0169 |
-0.1909 |
0.0169 |
0.0208 |
-0.1859 |
0.0208 |
0.0246 |
-0.1837 |
0.0246 |
0.0283 |
-0.1787 |
0.0283 |
0.0320 |
-0.1749 |
0.0320 |
0.0357 |
-0.1720 |
0.0357 |
0.0393 |
-0.1690 |
0.0393 |
0.0429 |
-0.1649 |
0.0429 |
0.0465 |
-0.1617 |
0.0465 |
0.0500 |
-0.1585 |
0.0500 |
0.0535 |
-0.1540 |
0.0535 |
0.0569 |
-0.1521 |
0.0569 |
0.0603 |
-0.1488 |
0.0603 |
0.0636 |
-0.1462 |
0.0669 |
0.0702 |
-0.1406 |
Excess molar heat capacity, J/K/mol
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,3-Propanediol (1) - Liquid |
Excess molar heat capacity, J/K/mol - Liquid |
283.15 |
0.0248 |
1.28 |
283.15 |
0.0369 |
1.89 |
283.15 |
0.0502 |
2.35 |
283.15 |
0.0751 |
2.54 |
283.15 |
0.1401 |
2.24 |
283.15 |
0.1504 |
2.2 |
283.15 |
0.2990 |
1.59 |
283.15 |
0.3982 |
1.31 |
283.15 |
0.4976 |
1.26 |
283.15 |
0.5955 |
1.15 |
283.15 |
0.7902 |
0.9800 |
283.15 |
0.9455 |
0.4800 |
293.15 |
0.0248 |
1.4 |
293.15 |
0.0369 |
2.08 |
293.15 |
0.0502 |
2.72 |
293.15 |
0.0751 |
3.22 |
293.15 |
0.1401 |
3.61 |
293.15 |
0.1504 |
3.67 |
293.15 |
0.2990 |
3.18 |
293.15 |
0.3982 |
2.66 |
293.15 |
0.4976 |
2.34 |
293.15 |
0.5955 |
1.92 |
293.15 |
0.7025 |
1.71 |
293.15 |
0.7902 |
1.19 |
293.15 |
0.9455 |
0.5300 |
298.15 |
0.0248 |
1.43 |
298.15 |
0.0369 |
2.13 |
298.15 |
0.0502 |
2.83 |
298.15 |
0.0751 |
3.44 |
298.15 |
0.1401 |
4.11 |
298.15 |
0.1504 |
4.21 |
298.15 |
0.2990 |
3.84 |
298.15 |
0.3982 |
3.28 |
298.15 |
0.4976 |
2.82 |
298.15 |
0.5955 |
2.33 |
298.15 |
0.7025 |
1.95 |
298.15 |
0.7902 |
1.3 |
298.15 |
0.9455 |
0.5800 |
303.15 |
0.0248 |
1.44 |
303.15 |
0.0369 |
2.16 |
303.15 |
0.0502 |
2.9 |
303.15 |
0.0751 |
3.59 |
303.15 |
0.1401 |
4.52 |
303.15 |
0.1504 |
4.64 |
303.15 |
0.2990 |
4.43 |
303.15 |
0.3982 |
3.85 |
303.15 |
0.4976 |
3.25 |
303.15 |
0.5955 |
2.74 |
303.15 |
0.7025 |
2.2 |
303.15 |
0.7902 |
1.4 |
303.15 |
0.9455 |
0.6100 |
313.15 |
0.0248 |
1.46 |
313.15 |
0.0369 |
2.26 |
313.15 |
0.0502 |
2.99 |
313.15 |
0.0751 |
3.8 |
313.15 |
0.1401 |
5.08 |
313.15 |
0.1504 |
5.27 |
313.15 |
0.2990 |
5.44 |
313.15 |
0.3982 |
4.81 |
313.15 |
0.4976 |
4.02 |
313.15 |
0.5955 |
3.48 |
313.15 |
0.7025 |
2.64 |
313.15 |
0.7902 |
1.49 |
313.15 |
0.9455 |
0.5500 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,3-Propanediol (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 |
0.0272 |
-0.2360 |
298.15 |
0.0591 |
-0.4530 |
298.15 |
0.1239 |
-0.7440 |
298.15 |
0.2087 |
-0.9240 |
298.15 |
0.3088 |
-1.011 |
298.15 |
0.3926 |
-1.034 |
298.15 |
0.5013 |
-0.9920 |
298.15 |
0.5510 |
-0.9040 |
298.15 |
0.6483 |
-0.7890 |
298.15 |
0.7430 |
-0.6330 |
298.15 |
0.8269 |
-0.4580 |
298.15 |
0.9249 |
-0.2560 |
323.15 |
0.0272 |
-0.1670 |
323.15 |
0.0591 |
-0.3200 |
323.15 |
0.1239 |
-0.5330 |
323.15 |
0.2087 |
-0.7300 |
323.15 |
0.3088 |
-0.8310 |
323.15 |
0.3926 |
-0.8320 |
323.15 |
0.5013 |
-0.8210 |
323.15 |
0.5510 |
-0.8130 |
323.15 |
0.6483 |
-0.7350 |
323.15 |
0.7430 |
-0.5840 |
323.15 |
0.8269 |
-0.4170 |
323.15 |
0.9249 |
-0.1950 |
343.15 |
0.0272 |
-0.1250 |
343.15 |
0.0591 |
-0.2290 |
343.15 |
0.1239 |
-0.3860 |
343.15 |
0.2087 |
-0.4640 |
343.15 |
0.3088 |
-0.5600 |
343.15 |
0.3926 |
-0.5910 |
343.15 |
0.5013 |
-0.5930 |
343.15 |
0.5510 |
-0.5790 |
343.15 |
0.6483 |
-0.5050 |
343.15 |
0.7430 |
-0.4330 |
343.15 |
0.8269 |
-0.3080 |
343.15 |
0.9249 |
-0.1530 |
Molar enthalpy of dilution, kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Fixed |
Measured |
Initial molality of solute, mol/kg - Liquid |
Final molality of solute, mol/kg - Liquid |
Molar enthalpy of dilution, kJ/mol - Liquid |
0.0012 |
0.0052 |
-0.2008 |
0.0052 |
0.0092 |
-0.1978 |
0.0092 |
0.0131 |
-0.1936 |
0.0131 |
0.0169 |
-0.1909 |
0.0169 |
0.0208 |
-0.1859 |
0.0208 |
0.0246 |
-0.1837 |
0.0246 |
0.0283 |
-0.1787 |
0.0283 |
0.0320 |
-0.1749 |
0.0320 |
0.0357 |
-0.1720 |
0.0357 |
0.0393 |
-0.1690 |
0.0393 |
0.0429 |
-0.1649 |
0.0429 |
0.0465 |
-0.1617 |
0.0465 |
0.0500 |
-0.1585 |
0.0500 |
0.0535 |
-0.1540 |
0.0535 |
0.0569 |
-0.1521 |
0.0569 |
0.0603 |
-0.1488 |
0.0603 |
0.0636 |
-0.1462 |
0.0669 |
0.0702 |
-0.1406 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
273.15 |
0.1052 |
0.06 |
273.15 |
0.2088 |
0.10 |
273.15 |
0.3623 |
0.20 |
273.15 |
0.5000 |
0.29 |
273.15 |
0.6250 |
0.37 |
273.15 |
0.7500 |
0.44 |
273.15 |
0.8000 |
0.48 |
273.15 |
0.9000 |
0.52 |
273.15 |
1.0000 |
0.59 |
283.15 |
0.1052 |
0.12 |
283.15 |
0.2088 |
0.20 |
283.15 |
0.3623 |
0.41 |
283.15 |
0.5000 |
0.59 |
283.15 |
0.6250 |
0.76 |
283.15 |
0.7500 |
0.90 |
283.15 |
0.8000 |
0.98 |
283.15 |
0.9000 |
1.07 |
283.15 |
1.0000 |
1.21 |
293.15 |
0.1052 |
0.23 |
293.15 |
0.2088 |
0.40 |
293.15 |
0.3623 |
0.80 |
293.15 |
0.5000 |
1.16 |
293.15 |
0.6250 |
1.48 |
293.15 |
0.7500 |
1.74 |
293.15 |
0.8000 |
1.88 |
293.15 |
0.9000 |
2.07 |
293.15 |
1.0000 |
2.33 |
303.15 |
0.1052 |
0.42 |
303.15 |
0.2088 |
0.74 |
303.15 |
0.3623 |
1.47 |
303.15 |
0.5000 |
2.14 |
303.15 |
0.6250 |
2.71 |
303.15 |
0.7500 |
3.18 |
303.15 |
0.8000 |
3.45 |
303.15 |
0.9000 |
3.79 |
303.15 |
1.0000 |
4.25 |
313.15 |
0.1052 |
0.73 |
313.15 |
0.2088 |
1.31 |
313.15 |
0.3623 |
2.59 |
313.15 |
0.5000 |
3.77 |
313.15 |
0.6250 |
4.76 |
313.15 |
0.7500 |
5.58 |
313.15 |
0.8000 |
6.03 |
313.15 |
0.9000 |
6.63 |
313.15 |
1.0000 |
7.41 |
323.15 |
0.1052 |
1.23 |
323.15 |
0.2088 |
2.25 |
323.15 |
0.3623 |
4.38 |
323.15 |
0.5000 |
6.38 |
323.15 |
0.6250 |
8.03 |
323.15 |
0.7500 |
9.40 |
323.15 |
0.8000 |
10.14 |
323.15 |
0.9000 |
11.14 |
323.15 |
1.0000 |
12.40 |
333.15 |
0.1052 |
2.00 |
333.15 |
0.2088 |
3.70 |
333.15 |
0.3623 |
7.15 |
333.15 |
0.5000 |
10.41 |
333.15 |
0.6250 |
13.06 |
333.15 |
0.7500 |
15.26 |
333.15 |
0.8000 |
16.44 |
333.15 |
0.9000 |
18.03 |
333.15 |
1.0000 |
20.00 |
343.15 |
0.1052 |
3.17 |
343.15 |
0.2088 |
5.91 |
343.15 |
0.3623 |
11.30 |
343.15 |
0.5000 |
16.41 |
343.15 |
0.6250 |
20.54 |
343.15 |
0.7500 |
23.96 |
343.15 |
0.8000 |
25.79 |
343.15 |
0.9000 |
28.25 |
343.15 |
1.0000 |
31.21 |
353.15 |
0.1052 |
4.87 |
353.15 |
0.2088 |
9.15 |
353.15 |
0.3623 |
17.36 |
353.15 |
0.5000 |
25.11 |
353.15 |
0.6250 |
31.38 |
353.15 |
0.7500 |
36.55 |
353.15 |
0.8000 |
39.28 |
353.15 |
0.9000 |
42.97 |
353.15 |
1.0000 |
47.30 |
363.15 |
0.1052 |
7.31 |
363.15 |
0.2088 |
13.79 |
363.15 |
0.3623 |
25.97 |
363.15 |
0.5000 |
37.38 |
363.15 |
0.6250 |
46.66 |
363.15 |
0.7500 |
54.27 |
363.15 |
0.8000 |
58.27 |
363.15 |
0.9000 |
63.62 |
363.15 |
1.0000 |
69.77 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
273.15 |
0.1052 |
0.06 |
273.15 |
0.2088 |
0.10 |
273.15 |
0.3623 |
0.20 |
273.15 |
0.5000 |
0.29 |
273.15 |
0.6250 |
0.37 |
273.15 |
0.7500 |
0.44 |
273.15 |
0.8000 |
0.48 |
273.15 |
0.9000 |
0.52 |
273.15 |
1.0000 |
0.59 |
283.15 |
0.1052 |
0.12 |
283.15 |
0.2088 |
0.20 |
283.15 |
0.3623 |
0.41 |
283.15 |
0.5000 |
0.59 |
283.15 |
0.6250 |
0.76 |
283.15 |
0.7500 |
0.90 |
283.15 |
0.8000 |
0.98 |
283.15 |
0.9000 |
1.07 |
283.15 |
1.0000 |
1.21 |
293.15 |
0.1052 |
0.23 |
293.15 |
0.2088 |
0.40 |
293.15 |
0.3623 |
0.80 |
293.15 |
0.5000 |
1.16 |
293.15 |
0.6250 |
1.48 |
293.15 |
0.7500 |
1.74 |
293.15 |
0.8000 |
1.88 |
293.15 |
0.9000 |
2.07 |
293.15 |
1.0000 |
2.33 |
303.15 |
0.1052 |
0.42 |
303.15 |
0.2088 |
0.74 |
303.15 |
0.3623 |
1.47 |
303.15 |
0.5000 |
2.14 |
303.15 |
0.6250 |
2.71 |
303.15 |
0.7500 |
3.18 |
303.15 |
0.8000 |
3.45 |
303.15 |
0.9000 |
3.79 |
303.15 |
1.0000 |
4.25 |
313.15 |
0.1052 |
0.73 |
313.15 |
0.2088 |
1.31 |
313.15 |
0.3623 |
2.59 |
313.15 |
0.5000 |
3.77 |
313.15 |
0.6250 |
4.76 |
313.15 |
0.7500 |
5.58 |
313.15 |
0.8000 |
6.03 |
313.15 |
0.9000 |
6.63 |
313.15 |
1.0000 |
7.41 |
323.15 |
0.1052 |
1.23 |
323.15 |
0.2088 |
2.25 |
323.15 |
0.3623 |
4.38 |
323.15 |
0.5000 |
6.38 |
323.15 |
0.6250 |
8.03 |
323.15 |
0.7500 |
9.40 |
323.15 |
0.8000 |
10.14 |
323.15 |
0.9000 |
11.14 |
323.15 |
1.0000 |
12.40 |
333.15 |
0.1052 |
2.00 |
333.15 |
0.2088 |
3.70 |
333.15 |
0.3623 |
7.15 |
333.15 |
0.5000 |
10.41 |
333.15 |
0.6250 |
13.06 |
333.15 |
0.7500 |
15.26 |
333.15 |
0.8000 |
16.44 |
333.15 |
0.9000 |
18.03 |
333.15 |
1.0000 |
20.00 |
343.15 |
0.1052 |
3.17 |
343.15 |
0.2088 |
5.91 |
343.15 |
0.3623 |
11.30 |
343.15 |
0.5000 |
16.41 |
343.15 |
0.6250 |
20.54 |
343.15 |
0.7500 |
23.96 |
343.15 |
0.8000 |
25.79 |
343.15 |
0.9000 |
28.25 |
343.15 |
1.0000 |
31.21 |
353.15 |
0.1052 |
4.87 |
353.15 |
0.2088 |
9.15 |
353.15 |
0.3623 |
17.36 |
353.15 |
0.5000 |
25.11 |
353.15 |
0.6250 |
31.38 |
353.15 |
0.7500 |
36.55 |
353.15 |
0.8000 |
39.28 |
353.15 |
0.9000 |
42.97 |
353.15 |
1.0000 |
47.30 |
363.15 |
0.1052 |
7.31 |
363.15 |
0.2088 |
13.79 |
363.15 |
0.3623 |
25.97 |
363.15 |
0.5000 |
37.38 |
363.15 |
0.6250 |
46.66 |
363.15 |
0.7500 |
54.27 |
363.15 |
0.8000 |
58.27 |
363.15 |
0.9000 |
63.62 |
363.15 |
1.0000 |
69.77 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of 1,3-Propanediol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
278.15 |
0.0000 |
1.3341 |
278.15 |
0.1113 |
1.3466 |
278.15 |
0.2226 |
1.3599 |
278.15 |
0.3340 |
1.374 |
278.15 |
0.4453 |
1.3866 |
278.15 |
0.5010 |
1.3931 |
278.15 |
0.6123 |
1.4066 |
278.15 |
0.7236 |
1.4181 |
278.15 |
0.8349 |
1.4289 |
278.15 |
0.9277 |
1.4371 |
278.15 |
1.0000 |
1.4436 |
283.15 |
0.0000 |
1.3338 |
283.15 |
0.1113 |
1.3462 |
283.15 |
0.2226 |
1.3592 |
283.15 |
0.3340 |
1.3729 |
283.15 |
0.4453 |
1.3856 |
283.15 |
0.5010 |
1.3921 |
283.15 |
0.6123 |
1.4055 |
283.15 |
0.7236 |
1.4169 |
283.15 |
0.8349 |
1.4276 |
283.15 |
0.9277 |
1.4358 |
283.15 |
1.0000 |
1.4423 |
288.15 |
0.0000 |
1.3335 |
288.15 |
0.1113 |
1.3457 |
288.15 |
0.2226 |
1.3586 |
288.15 |
0.3340 |
1.3719 |
288.15 |
0.4453 |
1.3845 |
288.15 |
0.5010 |
1.391 |
288.15 |
0.6123 |
1.4041 |
288.15 |
0.7236 |
1.4157 |
288.15 |
0.8349 |
1.4263 |
288.15 |
0.9277 |
1.4345 |
288.15 |
1.0000 |
1.4409 |
293.15 |
0.0000 |
1.3331 |
293.15 |
0.1113 |
1.3452 |
293.15 |
0.2226 |
1.3579 |
293.15 |
0.3340 |
1.371 |
293.15 |
0.4453 |
1.3835 |
293.15 |
0.5010 |
1.3899 |
293.15 |
0.6123 |
1.4029 |
293.15 |
0.7236 |
1.4145 |
293.15 |
0.8349 |
1.425 |
293.15 |
0.9277 |
1.4332 |
293.15 |
1.0000 |
1.4395 |
298.15 |
0.0000 |
1.3326 |
298.15 |
0.1113 |
1.3446 |
298.15 |
0.2226 |
1.3572 |
298.15 |
0.3340 |
1.3702 |
298.15 |
0.4453 |
1.3825 |
298.15 |
0.5010 |
1.3888 |
298.15 |
0.6123 |
1.4015 |
298.15 |
0.7236 |
1.4133 |
298.15 |
0.8349 |
1.4237 |
298.15 |
0.9277 |
1.4319 |
298.15 |
1.0000 |
1.4381 |
303.15 |
0.0000 |
1.332 |
303.15 |
0.1113 |
1.344 |
303.15 |
0.2226 |
1.3564 |
303.15 |
0.3340 |
1.3693 |
303.15 |
0.4453 |
1.3815 |
303.15 |
0.5010 |
1.3876 |
303.15 |
0.6123 |
1.4002 |
303.15 |
0.7236 |
1.4118 |
303.15 |
0.8349 |
1.4224 |
303.15 |
0.9277 |
1.4304 |
303.15 |
1.0000 |
1.4368 |
308.15 |
0.0000 |
1.3313 |
308.15 |
0.1113 |
1.3434 |
308.15 |
0.2226 |
1.3558 |
308.15 |
0.3340 |
1.3684 |
308.15 |
0.4453 |
1.3804 |
308.15 |
0.5010 |
1.3865 |
308.15 |
0.6123 |
1.3989 |
308.15 |
0.7236 |
1.4103 |
308.15 |
0.8349 |
1.4211 |
308.15 |
0.9277 |
1.4289 |
308.15 |
1.0000 |
1.4354 |
313.15 |
0.0000 |
1.3306 |
313.15 |
0.1113 |
1.3426 |
313.15 |
0.2226 |
1.355 |
313.15 |
0.3340 |
1.3676 |
313.15 |
0.4453 |
1.3793 |
313.15 |
0.5010 |
1.3854 |
313.15 |
0.6123 |
1.3977 |
313.15 |
0.7236 |
1.4089 |
313.15 |
0.8349 |
1.4197 |
313.15 |
0.9277 |
1.4275 |
313.15 |
1.0000 |
1.434 |
318.15 |
0.0000 |
1.3298 |
318.15 |
0.1113 |
1.3418 |
318.15 |
0.2226 |
1.3541 |
318.15 |
0.3340 |
1.3668 |
318.15 |
0.4453 |
1.3782 |
318.15 |
0.5010 |
1.3845 |
318.15 |
0.6123 |
1.3965 |
318.15 |
0.7236 |
1.4075 |
318.15 |
0.8349 |
1.4182 |
318.15 |
0.9277 |
1.4261 |
318.15 |
1.0000 |
1.4325 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of 1,3-Propanediol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
278.15 |
0.0000 |
1.3341 |
278.15 |
0.1113 |
1.3466 |
278.15 |
0.2226 |
1.3599 |
278.15 |
0.3340 |
1.374 |
278.15 |
0.4453 |
1.3866 |
278.15 |
0.5010 |
1.3931 |
278.15 |
0.6123 |
1.4066 |
278.15 |
0.7236 |
1.4181 |
278.15 |
0.8349 |
1.4289 |
278.15 |
0.9277 |
1.4371 |
278.15 |
1.0000 |
1.4436 |
283.15 |
0.0000 |
1.3338 |
283.15 |
0.1113 |
1.3462 |
283.15 |
0.2226 |
1.3592 |
283.15 |
0.3340 |
1.3729 |
283.15 |
0.4453 |
1.3856 |
283.15 |
0.5010 |
1.3921 |
283.15 |
0.6123 |
1.4055 |
283.15 |
0.7236 |
1.4169 |
283.15 |
0.8349 |
1.4276 |
283.15 |
0.9277 |
1.4358 |
283.15 |
1.0000 |
1.4423 |
288.15 |
0.0000 |
1.3335 |
288.15 |
0.1113 |
1.3457 |
288.15 |
0.2226 |
1.3586 |
288.15 |
0.3340 |
1.3719 |
288.15 |
0.4453 |
1.3845 |
288.15 |
0.5010 |
1.391 |
288.15 |
0.6123 |
1.4041 |
288.15 |
0.7236 |
1.4157 |
288.15 |
0.8349 |
1.4263 |
288.15 |
0.9277 |
1.4345 |
288.15 |
1.0000 |
1.4409 |
293.15 |
0.0000 |
1.3331 |
293.15 |
0.1113 |
1.3452 |
293.15 |
0.2226 |
1.3579 |
293.15 |
0.3340 |
1.371 |
293.15 |
0.4453 |
1.3835 |
293.15 |
0.5010 |
1.3899 |
293.15 |
0.6123 |
1.4029 |
293.15 |
0.7236 |
1.4145 |
293.15 |
0.8349 |
1.425 |
293.15 |
0.9277 |
1.4332 |
293.15 |
1.0000 |
1.4395 |
298.15 |
0.0000 |
1.3326 |
298.15 |
0.1113 |
1.3446 |
298.15 |
0.2226 |
1.3572 |
298.15 |
0.3340 |
1.3702 |
298.15 |
0.4453 |
1.3825 |
298.15 |
0.5010 |
1.3888 |
298.15 |
0.6123 |
1.4015 |
298.15 |
0.7236 |
1.4133 |
298.15 |
0.8349 |
1.4237 |
298.15 |
0.9277 |
1.4319 |
298.15 |
1.0000 |
1.4381 |
303.15 |
0.0000 |
1.332 |
303.15 |
0.1113 |
1.344 |
303.15 |
0.2226 |
1.3564 |
303.15 |
0.3340 |
1.3693 |
303.15 |
0.4453 |
1.3815 |
303.15 |
0.5010 |
1.3876 |
303.15 |
0.6123 |
1.4002 |
303.15 |
0.7236 |
1.4118 |
303.15 |
0.8349 |
1.4224 |
303.15 |
0.9277 |
1.4304 |
303.15 |
1.0000 |
1.4368 |
308.15 |
0.0000 |
1.3313 |
308.15 |
0.1113 |
1.3434 |
308.15 |
0.2226 |
1.3558 |
308.15 |
0.3340 |
1.3684 |
308.15 |
0.4453 |
1.3804 |
308.15 |
0.5010 |
1.3865 |
308.15 |
0.6123 |
1.3989 |
308.15 |
0.7236 |
1.4103 |
308.15 |
0.8349 |
1.4211 |
308.15 |
0.9277 |
1.4289 |
308.15 |
1.0000 |
1.4354 |
313.15 |
0.0000 |
1.3306 |
313.15 |
0.1113 |
1.3426 |
313.15 |
0.2226 |
1.355 |
313.15 |
0.3340 |
1.3676 |
313.15 |
0.4453 |
1.3793 |
313.15 |
0.5010 |
1.3854 |
313.15 |
0.6123 |
1.3977 |
313.15 |
0.7236 |
1.4089 |
313.15 |
0.8349 |
1.4197 |
313.15 |
0.9277 |
1.4275 |
313.15 |
1.0000 |
1.434 |
318.15 |
0.0000 |
1.3298 |
318.15 |
0.1113 |
1.3418 |
318.15 |
0.2226 |
1.3541 |
318.15 |
0.3340 |
1.3668 |
318.15 |
0.4453 |
1.3782 |
318.15 |
0.5010 |
1.3845 |
318.15 |
0.6123 |
1.3965 |
318.15 |
0.7236 |
1.4075 |
318.15 |
0.8349 |
1.4182 |
318.15 |
0.9277 |
1.4261 |
318.15 |
1.0000 |
1.4325 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of 1,3-Propanediol (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0731 |
1015.1 |
0.1555 |
1028.5 |
0.2449 |
1038.2 |
0.3384 |
1044.4 |
0.4321 |
1047.9 |
0.5223 |
1049.6 |
0.6058 |
1050.3 |
0.6803 |
1050.4 |
0.7446 |
1050.5 |
0.7987 |
1050.5 |
0.8430 |
1050.4 |
0.8786 |
1050.4 |
0.9068 |
1050.2 |
0.9355 |
1049.9 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.0000 |
1058.85 |
283.15 |
0.1022 |
1059.27 |
283.15 |
0.2010 |
1059.47 |
283.15 |
0.2987 |
1059.49 |
283.15 |
0.3998 |
1059.07 |
283.15 |
0.4997 |
1057.91 |
283.15 |
0.5997 |
1055.48 |
283.15 |
0.6999 |
1050.47 |
283.15 |
0.7999 |
1041.86 |
283.15 |
0.8997 |
1025.27 |
283.15 |
1.0000 |
999.68 |
293.15 |
0.0000 |
1052.61 |
293.15 |
0.1022 |
1053.04 |
293.15 |
0.2010 |
1053.26 |
293.15 |
0.2987 |
1053.3 |
293.15 |
0.3998 |
1052.91 |
293.15 |
0.4997 |
1051.82 |
293.15 |
0.5997 |
1049.54 |
293.15 |
0.6999 |
1044.85 |
293.15 |
0.7999 |
1036.89 |
293.15 |
0.8997 |
1021.75 |
293.15 |
1.0000 |
998.19 |
303.15 |
0.0000 |
1046.36 |
303.15 |
0.1022 |
1046.79 |
303.15 |
0.2010 |
1047.01 |
303.15 |
0.2987 |
1047.05 |
303.15 |
0.3998 |
1046.67 |
303.15 |
0.4997 |
1045.61 |
303.15 |
0.5997 |
1043.42 |
303.15 |
0.6999 |
1039.01 |
303.15 |
0.7999 |
1031.59 |
303.15 |
0.8997 |
1017.64 |
303.15 |
1.0000 |
995.64 |
313.15 |
0.0000 |
1040.07 |
313.15 |
0.1022 |
1040.48 |
313.15 |
0.2010 |
1040.68 |
313.15 |
0.2987 |
1040.7 |
313.15 |
0.3998 |
1040.3 |
313.15 |
0.4997 |
1039.25 |
313.15 |
0.5997 |
1037.1 |
313.15 |
0.6999 |
1032.92 |
313.15 |
0.7999 |
1025.94 |
313.15 |
0.8997 |
1012.95 |
313.15 |
1.0000 |
992.17 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of 1,3-Propanediol (1) - Liquid |
Mass density, kg/m3 - Liquid |
273.15 |
0.0000 |
1000.8 |
273.15 |
0.1113 |
1009.7 |
273.15 |
0.2226 |
1021.3 |
273.15 |
0.3340 |
1032.5 |
273.15 |
0.4453 |
1043.7 |
273.15 |
0.5010 |
1048.1 |
273.15 |
0.6123 |
1056.9 |
273.15 |
0.7236 |
1062.7 |
273.15 |
0.8349 |
1066.3 |
273.15 |
0.9277 |
1067.1 |
273.15 |
1.0000 |
1065.9 |
283.15 |
0.0000 |
1000.6 |
283.15 |
0.1113 |
1008.8 |
283.15 |
0.2226 |
1019.2 |
283.15 |
0.3340 |
1029.2 |
283.15 |
0.4453 |
1039.3 |
283.15 |
0.5010 |
1043.3 |
283.15 |
0.6123 |
1051.4 |
283.15 |
0.7236 |
1056.8 |
283.15 |
0.8349 |
1060.2 |
283.15 |
0.9277 |
1061.0 |
283.15 |
1.0000 |
1059.8 |
293.15 |
0.0000 |
999.3 |
293.15 |
0.1113 |
1006.7 |
293.15 |
0.2226 |
1016.3 |
293.15 |
0.3340 |
1025.4 |
293.15 |
0.4453 |
1034.5 |
293.15 |
0.5010 |
1038.3 |
293.15 |
0.6123 |
1045.7 |
293.15 |
0.7236 |
1050.9 |
293.15 |
0.8349 |
1054.0 |
293.15 |
0.9277 |
1054.7 |
293.15 |
1.0000 |
1053.6 |
303.15 |
0.0000 |
996.8 |
303.15 |
0.1113 |
1004.1 |
303.15 |
0.2226 |
1012.9 |
303.15 |
0.3340 |
1021.1 |
303.15 |
0.4453 |
1029.5 |
303.15 |
0.5010 |
1033.0 |
303.15 |
0.6123 |
1039.9 |
303.15 |
0.7236 |
1044.8 |
303.15 |
0.8349 |
1047.8 |
303.15 |
0.9277 |
1048.5 |
303.15 |
1.0000 |
1047.4 |
313.15 |
0.0000 |
993.2 |
313.15 |
0.1113 |
1000.4 |
313.15 |
0.2226 |
1008.3 |
313.15 |
0.3340 |
1016.3 |
313.15 |
0.4453 |
1023.9 |
313.15 |
0.5010 |
1027.3 |
313.15 |
0.6123 |
1033.8 |
313.15 |
0.7236 |
1038.6 |
313.15 |
0.8349 |
1041.5 |
313.15 |
0.9277 |
1042.2 |
313.15 |
1.0000 |
1041.1 |
323.15 |
0.0000 |
989.0 |
323.15 |
0.1113 |
996.2 |
323.15 |
0.2226 |
1003.5 |
323.15 |
0.3340 |
1010.8 |
323.15 |
0.4453 |
1018.1 |
323.15 |
0.5010 |
1021.3 |
323.15 |
0.6123 |
1027.4 |
323.15 |
0.7236 |
1032.1 |
323.15 |
0.8349 |
1035.0 |
323.15 |
0.9277 |
1035.8 |
323.15 |
1.0000 |
1034.8 |
333.15 |
0.0000 |
984.4 |
333.15 |
0.1113 |
991.1 |
333.15 |
0.2226 |
998.3 |
333.15 |
0.3340 |
1005.2 |
333.15 |
0.4453 |
1011.8 |
333.15 |
0.5010 |
1014.8 |
333.15 |
0.6123 |
1020.9 |
333.15 |
0.7236 |
1025.4 |
333.15 |
0.8349 |
1028.3 |
333.15 |
0.9277 |
1029.3 |
333.15 |
1.0000 |
1028.4 |
343.15 |
0.0000 |
978.6 |
343.15 |
0.1113 |
985.3 |
343.15 |
0.2226 |
992.4 |
343.15 |
0.3340 |
999.3 |
343.15 |
0.4453 |
1005.3 |
343.15 |
0.5010 |
1008.4 |
343.15 |
0.6123 |
1014.1 |
343.15 |
0.7236 |
1018.5 |
343.15 |
0.8349 |
1021.5 |
343.15 |
0.9277 |
1022.6 |
343.15 |
1.0000 |
1021.9 |
353.15 |
0.0000 |
972.7 |
353.15 |
0.1113 |
978.6 |
353.15 |
0.2226 |
986.3 |
353.15 |
0.3340 |
992.6 |
353.15 |
0.4453 |
998.5 |
353.15 |
0.5010 |
1001.2 |
353.15 |
0.6123 |
1006.8 |
353.15 |
0.7236 |
1011.7 |
353.15 |
0.8349 |
1014.4 |
353.15 |
0.9277 |
1015.8 |
353.15 |
1.0000 |
1015.3 |
253.15 |
0.4453 |
1053.7 |
253.15 |
0.5010 |
1058.0 |
253.15 |
0.6123 |
1068.2 |
253.15 |
0.7236 |
1074.9 |
253.15 |
0.8349 |
1078.5 |
253.15 |
0.9277 |
1079.6 |
253.15 |
1.0000 |
1078.2 |
258.15 |
0.4453 |
1051.8 |
258.15 |
0.5010 |
1055.9 |
258.15 |
0.6123 |
1065.8 |
258.15 |
0.7236 |
1072.2 |
258.15 |
0.8349 |
1075.5 |
258.15 |
0.9277 |
1076.5 |
258.15 |
1.0000 |
1075.4 |
263.15 |
0.3340 |
1035.2 |
263.15 |
0.4453 |
1047.7 |
263.15 |
0.5010 |
1052.5 |
263.15 |
0.6123 |
1062.1 |
263.15 |
0.7236 |
1068.4 |
263.15 |
0.8349 |
1072.2 |
263.15 |
0.9277 |
1073.2 |
263.15 |
1.0000 |
1072.3 |
268.15 |
0.2226 |
1022.1 |
268.15 |
0.3340 |
1033.9 |
268.15 |
0.4453 |
1045.7 |
268.15 |
0.5010 |
1050.3 |
268.15 |
0.6123 |
1059.5 |
268.15 |
0.7236 |
1065.6 |
268.15 |
0.8349 |
1069.3 |
268.15 |
0.9277 |
1070.1 |
268.15 |
1.0000 |
1069.0 |
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 |
0.0622 |
1050.19 |
298.15 |
0.1496 |
1050.32 |
298.15 |
0.2563 |
1050.38 |
298.15 |
0.3500 |
1050.3 |
298.15 |
0.4555 |
1049.74 |
298.15 |
0.5000 |
1049.21 |
298.15 |
0.5548 |
1048.18 |
298.15 |
0.6522 |
1044.85 |
298.15 |
0.7553 |
1038.16 |
298.15 |
0.8522 |
1027.32 |
298.15 |
0.9085 |
1018.19 |
298.15 |
0.9147 |
1017.03 |
298.15 |
0.9255 |
1014.92 |
298.15 |
0.9350 |
1012.97 |
298.15 |
0.9548 |
1008.63 |
298.15 |
0.9556 |
1008.44 |
298.15 |
0.9602 |
1007.37 |
298.15 |
0.9700 |
1005.0 |
298.15 |
0.9801 |
1002.45 |
298.15 |
0.9897 |
999.9 |
298.15 |
0.9921 |
999.25 |
298.15 |
0.9951 |
998.42 |
308.15 |
0.0622 |
1043.88 |
308.15 |
0.1496 |
1044.01 |
308.15 |
0.2563 |
1044.07 |
308.15 |
0.3500 |
1043.97 |
308.15 |
0.4555 |
1043.39 |
308.15 |
0.5000 |
1042.86 |
308.15 |
0.5548 |
1041.87 |
308.15 |
0.6522 |
1038.75 |
308.15 |
0.7553 |
1032.55 |
308.15 |
0.8522 |
1022.53 |
308.15 |
0.9085 |
1014.02 |
308.15 |
0.9147 |
1012.94 |
308.15 |
0.9255 |
1010.96 |
308.15 |
0.9350 |
1009.13 |
308.15 |
0.9548 |
1005.04 |
308.15 |
0.9556 |
1004.87 |
308.15 |
0.9602 |
1003.85 |
308.15 |
0.9700 |
1001.61 |
308.15 |
0.9801 |
999.19 |
308.15 |
0.9897 |
996.76 |
308.15 |
0.9921 |
996.14 |
308.15 |
0.9951 |
995.35 |
318.15 |
0.0622 |
1037.53 |
318.15 |
0.1496 |
1037.64 |
318.15 |
0.2563 |
1037.68 |
318.15 |
0.3500 |
1037.55 |
318.15 |
0.4555 |
1036.94 |
318.15 |
0.5000 |
1036.42 |
318.15 |
0.5548 |
1035.46 |
318.15 |
0.6522 |
1032.48 |
318.15 |
0.7553 |
1026.64 |
318.15 |
0.8522 |
1017.23 |
318.15 |
0.9085 |
1009.22 |
318.15 |
0.9147 |
1008.19 |
318.15 |
0.9255 |
1006.32 |
318.15 |
0.9350 |
1004.59 |
318.15 |
0.9548 |
1000.71 |
318.15 |
0.9556 |
1000.54 |
318.15 |
0.9602 |
999.58 |
318.15 |
0.9700 |
997.45 |
318.15 |
0.9801 |
995.14 |
318.15 |
0.9897 |
992.82 |
318.15 |
0.9921 |
992.23 |
318.15 |
0.9951 |
991.47 |
328.15 |
0.0622 |
1031.1 |
328.15 |
0.1496 |
1031.18 |
328.15 |
0.2563 |
1031.17 |
328.15 |
0.3500 |
1030.98 |
328.15 |
0.4555 |
1030.32 |
328.15 |
0.5000 |
1029.79 |
328.15 |
0.5548 |
1028.83 |
328.15 |
0.6522 |
1025.94 |
328.15 |
0.7553 |
1020.39 |
328.15 |
0.8522 |
1011.49 |
328.15 |
0.9085 |
1003.89 |
328.15 |
0.9147 |
1002.92 |
328.15 |
0.9255 |
1001.14 |
328.15 |
0.9350 |
999.49 |
328.15 |
0.9548 |
995.78 |
328.15 |
0.9556 |
995.62 |
328.15 |
0.9602 |
994.7 |
328.15 |
0.9700 |
992.65 |
328.15 |
0.9801 |
990.44 |
328.15 |
0.9897 |
988.21 |
328.15 |
0.9921 |
987.63 |
328.15 |
0.9951 |
986.91 |
338.15 |
0.0622 |
1024.56 |
338.15 |
0.1496 |
1024.59 |
338.15 |
0.2563 |
1024.49 |
338.15 |
0.3500 |
1024.2 |
338.15 |
0.4555 |
1023.41 |
338.15 |
0.5000 |
1022.84 |
338.15 |
0.5548 |
1021.85 |
338.15 |
0.6522 |
1019.0 |
338.15 |
0.7553 |
1013.69 |
338.15 |
0.8522 |
1005.25 |
338.15 |
0.9085 |
998.04 |
338.15 |
0.9147 |
997.1 |
338.15 |
0.9255 |
995.41 |
338.15 |
0.9350 |
993.83 |
338.15 |
0.9548 |
990.28 |
338.15 |
0.9556 |
990.13 |
338.15 |
0.9602 |
989.24 |
338.15 |
0.9700 |
987.28 |
338.15 |
0.9801 |
985.14 |
338.15 |
0.9897 |
982.99 |
338.15 |
0.9921 |
982.43 |
338.15 |
0.9951 |
981.73 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of 1,3-Propanediol (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0731 |
1015.1 |
0.1555 |
1028.5 |
0.2449 |
1038.2 |
0.3384 |
1044.4 |
0.4321 |
1047.9 |
0.5223 |
1049.6 |
0.6058 |
1050.3 |
0.6803 |
1050.4 |
0.7446 |
1050.5 |
0.7987 |
1050.5 |
0.8430 |
1050.4 |
0.8786 |
1050.4 |
0.9068 |
1050.2 |
0.9355 |
1049.9 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.0000 |
1058.85 |
283.15 |
0.1022 |
1059.27 |
283.15 |
0.2010 |
1059.47 |
283.15 |
0.2987 |
1059.49 |
283.15 |
0.3998 |
1059.07 |
283.15 |
0.4997 |
1057.91 |
283.15 |
0.5997 |
1055.48 |
283.15 |
0.6999 |
1050.47 |
283.15 |
0.7999 |
1041.86 |
283.15 |
0.8997 |
1025.27 |
283.15 |
1.0000 |
999.68 |
293.15 |
0.0000 |
1052.61 |
293.15 |
0.1022 |
1053.04 |
293.15 |
0.2010 |
1053.26 |
293.15 |
0.2987 |
1053.3 |
293.15 |
0.3998 |
1052.91 |
293.15 |
0.4997 |
1051.82 |
293.15 |
0.5997 |
1049.54 |
293.15 |
0.6999 |
1044.85 |
293.15 |
0.7999 |
1036.89 |
293.15 |
0.8997 |
1021.75 |
293.15 |
1.0000 |
998.19 |
303.15 |
0.0000 |
1046.36 |
303.15 |
0.1022 |
1046.79 |
303.15 |
0.2010 |
1047.01 |
303.15 |
0.2987 |
1047.05 |
303.15 |
0.3998 |
1046.67 |
303.15 |
0.4997 |
1045.61 |
303.15 |
0.5997 |
1043.42 |
303.15 |
0.6999 |
1039.01 |
303.15 |
0.7999 |
1031.59 |
303.15 |
0.8997 |
1017.64 |
303.15 |
1.0000 |
995.64 |
313.15 |
0.0000 |
1040.07 |
313.15 |
0.1022 |
1040.48 |
313.15 |
0.2010 |
1040.68 |
313.15 |
0.2987 |
1040.7 |
313.15 |
0.3998 |
1040.3 |
313.15 |
0.4997 |
1039.25 |
313.15 |
0.5997 |
1037.1 |
313.15 |
0.6999 |
1032.92 |
313.15 |
0.7999 |
1025.94 |
313.15 |
0.8997 |
1012.95 |
313.15 |
1.0000 |
992.17 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of 1,3-Propanediol (1) - Liquid |
Mass density, kg/m3 - Liquid |
273.15 |
0.0000 |
1000.8 |
273.15 |
0.1113 |
1009.7 |
273.15 |
0.2226 |
1021.3 |
273.15 |
0.3340 |
1032.5 |
273.15 |
0.4453 |
1043.7 |
273.15 |
0.5010 |
1048.1 |
273.15 |
0.6123 |
1056.9 |
273.15 |
0.7236 |
1062.7 |
273.15 |
0.8349 |
1066.3 |
273.15 |
0.9277 |
1067.1 |
273.15 |
1.0000 |
1065.9 |
283.15 |
0.0000 |
1000.6 |
283.15 |
0.1113 |
1008.8 |
283.15 |
0.2226 |
1019.2 |
283.15 |
0.3340 |
1029.2 |
283.15 |
0.4453 |
1039.3 |
283.15 |
0.5010 |
1043.3 |
283.15 |
0.6123 |
1051.4 |
283.15 |
0.7236 |
1056.8 |
283.15 |
0.8349 |
1060.2 |
283.15 |
0.9277 |
1061.0 |
283.15 |
1.0000 |
1059.8 |
293.15 |
0.0000 |
999.3 |
293.15 |
0.1113 |
1006.7 |
293.15 |
0.2226 |
1016.3 |
293.15 |
0.3340 |
1025.4 |
293.15 |
0.4453 |
1034.5 |
293.15 |
0.5010 |
1038.3 |
293.15 |
0.6123 |
1045.7 |
293.15 |
0.7236 |
1050.9 |
293.15 |
0.8349 |
1054.0 |
293.15 |
0.9277 |
1054.7 |
293.15 |
1.0000 |
1053.6 |
303.15 |
0.0000 |
996.8 |
303.15 |
0.1113 |
1004.1 |
303.15 |
0.2226 |
1012.9 |
303.15 |
0.3340 |
1021.1 |
303.15 |
0.4453 |
1029.5 |
303.15 |
0.5010 |
1033.0 |
303.15 |
0.6123 |
1039.9 |
303.15 |
0.7236 |
1044.8 |
303.15 |
0.8349 |
1047.8 |
303.15 |
0.9277 |
1048.5 |
303.15 |
1.0000 |
1047.4 |
313.15 |
0.0000 |
993.2 |
313.15 |
0.1113 |
1000.4 |
313.15 |
0.2226 |
1008.3 |
313.15 |
0.3340 |
1016.3 |
313.15 |
0.4453 |
1023.9 |
313.15 |
0.5010 |
1027.3 |
313.15 |
0.6123 |
1033.8 |
313.15 |
0.7236 |
1038.6 |
313.15 |
0.8349 |
1041.5 |
313.15 |
0.9277 |
1042.2 |
313.15 |
1.0000 |
1041.1 |
323.15 |
0.0000 |
989.0 |
323.15 |
0.1113 |
996.2 |
323.15 |
0.2226 |
1003.5 |
323.15 |
0.3340 |
1010.8 |
323.15 |
0.4453 |
1018.1 |
323.15 |
0.5010 |
1021.3 |
323.15 |
0.6123 |
1027.4 |
323.15 |
0.7236 |
1032.1 |
323.15 |
0.8349 |
1035.0 |
323.15 |
0.9277 |
1035.8 |
323.15 |
1.0000 |
1034.8 |
333.15 |
0.0000 |
984.4 |
333.15 |
0.1113 |
991.1 |
333.15 |
0.2226 |
998.3 |
333.15 |
0.3340 |
1005.2 |
333.15 |
0.4453 |
1011.8 |
333.15 |
0.5010 |
1014.8 |
333.15 |
0.6123 |
1020.9 |
333.15 |
0.7236 |
1025.4 |
333.15 |
0.8349 |
1028.3 |
333.15 |
0.9277 |
1029.3 |
333.15 |
1.0000 |
1028.4 |
343.15 |
0.0000 |
978.6 |
343.15 |
0.1113 |
985.3 |
343.15 |
0.2226 |
992.4 |
343.15 |
0.3340 |
999.3 |
343.15 |
0.4453 |
1005.3 |
343.15 |
0.5010 |
1008.4 |
343.15 |
0.6123 |
1014.1 |
343.15 |
0.7236 |
1018.5 |
343.15 |
0.8349 |
1021.5 |
343.15 |
0.9277 |
1022.6 |
343.15 |
1.0000 |
1021.9 |
353.15 |
0.0000 |
972.7 |
353.15 |
0.1113 |
978.6 |
353.15 |
0.2226 |
986.3 |
353.15 |
0.3340 |
992.6 |
353.15 |
0.4453 |
998.5 |
353.15 |
0.5010 |
1001.2 |
353.15 |
0.6123 |
1006.8 |
353.15 |
0.7236 |
1011.7 |
353.15 |
0.8349 |
1014.4 |
353.15 |
0.9277 |
1015.8 |
353.15 |
1.0000 |
1015.3 |
253.15 |
0.4453 |
1053.7 |
253.15 |
0.5010 |
1058.0 |
253.15 |
0.6123 |
1068.2 |
253.15 |
0.7236 |
1074.9 |
253.15 |
0.8349 |
1078.5 |
253.15 |
0.9277 |
1079.6 |
253.15 |
1.0000 |
1078.2 |
258.15 |
0.4453 |
1051.8 |
258.15 |
0.5010 |
1055.9 |
258.15 |
0.6123 |
1065.8 |
258.15 |
0.7236 |
1072.2 |
258.15 |
0.8349 |
1075.5 |
258.15 |
0.9277 |
1076.5 |
258.15 |
1.0000 |
1075.4 |
263.15 |
0.3340 |
1035.2 |
263.15 |
0.4453 |
1047.7 |
263.15 |
0.5010 |
1052.5 |
263.15 |
0.6123 |
1062.1 |
263.15 |
0.7236 |
1068.4 |
263.15 |
0.8349 |
1072.2 |
263.15 |
0.9277 |
1073.2 |
263.15 |
1.0000 |
1072.3 |
268.15 |
0.2226 |
1022.1 |
268.15 |
0.3340 |
1033.9 |
268.15 |
0.4453 |
1045.7 |
268.15 |
0.5010 |
1050.3 |
268.15 |
0.6123 |
1059.5 |
268.15 |
0.7236 |
1065.6 |
268.15 |
0.8349 |
1069.3 |
268.15 |
0.9277 |
1070.1 |
268.15 |
1.0000 |
1069.0 |
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 |
0.0622 |
1050.19 |
298.15 |
0.1496 |
1050.32 |
298.15 |
0.2563 |
1050.38 |
298.15 |
0.3500 |
1050.3 |
298.15 |
0.4555 |
1049.74 |
298.15 |
0.5000 |
1049.21 |
298.15 |
0.5548 |
1048.18 |
298.15 |
0.6522 |
1044.85 |
298.15 |
0.7553 |
1038.16 |
298.15 |
0.8522 |
1027.32 |
298.15 |
0.9085 |
1018.19 |
298.15 |
0.9147 |
1017.03 |
298.15 |
0.9255 |
1014.92 |
298.15 |
0.9350 |
1012.97 |
298.15 |
0.9548 |
1008.63 |
298.15 |
0.9556 |
1008.44 |
298.15 |
0.9602 |
1007.37 |
298.15 |
0.9700 |
1005.0 |
298.15 |
0.9801 |
1002.45 |
298.15 |
0.9897 |
999.9 |
298.15 |
0.9921 |
999.25 |
298.15 |
0.9951 |
998.42 |
308.15 |
0.0622 |
1043.88 |
308.15 |
0.1496 |
1044.01 |
308.15 |
0.2563 |
1044.07 |
308.15 |
0.3500 |
1043.97 |
308.15 |
0.4555 |
1043.39 |
308.15 |
0.5000 |
1042.86 |
308.15 |
0.5548 |
1041.87 |
308.15 |
0.6522 |
1038.75 |
308.15 |
0.7553 |
1032.55 |
308.15 |
0.8522 |
1022.53 |
308.15 |
0.9085 |
1014.02 |
308.15 |
0.9147 |
1012.94 |
308.15 |
0.9255 |
1010.96 |
308.15 |
0.9350 |
1009.13 |
308.15 |
0.9548 |
1005.04 |
308.15 |
0.9556 |
1004.87 |
308.15 |
0.9602 |
1003.85 |
308.15 |
0.9700 |
1001.61 |
308.15 |
0.9801 |
999.19 |
308.15 |
0.9897 |
996.76 |
308.15 |
0.9921 |
996.14 |
308.15 |
0.9951 |
995.35 |
318.15 |
0.0622 |
1037.53 |
318.15 |
0.1496 |
1037.64 |
318.15 |
0.2563 |
1037.68 |
318.15 |
0.3500 |
1037.55 |
318.15 |
0.4555 |
1036.94 |
318.15 |
0.5000 |
1036.42 |
318.15 |
0.5548 |
1035.46 |
318.15 |
0.6522 |
1032.48 |
318.15 |
0.7553 |
1026.64 |
318.15 |
0.8522 |
1017.23 |
318.15 |
0.9085 |
1009.22 |
318.15 |
0.9147 |
1008.19 |
318.15 |
0.9255 |
1006.32 |
318.15 |
0.9350 |
1004.59 |
318.15 |
0.9548 |
1000.71 |
318.15 |
0.9556 |
1000.54 |
318.15 |
0.9602 |
999.58 |
318.15 |
0.9700 |
997.45 |
318.15 |
0.9801 |
995.14 |
318.15 |
0.9897 |
992.82 |
318.15 |
0.9921 |
992.23 |
318.15 |
0.9951 |
991.47 |
328.15 |
0.0622 |
1031.1 |
328.15 |
0.1496 |
1031.18 |
328.15 |
0.2563 |
1031.17 |
328.15 |
0.3500 |
1030.98 |
328.15 |
0.4555 |
1030.32 |
328.15 |
0.5000 |
1029.79 |
328.15 |
0.5548 |
1028.83 |
328.15 |
0.6522 |
1025.94 |
328.15 |
0.7553 |
1020.39 |
328.15 |
0.8522 |
1011.49 |
328.15 |
0.9085 |
1003.89 |
328.15 |
0.9147 |
1002.92 |
328.15 |
0.9255 |
1001.14 |
328.15 |
0.9350 |
999.49 |
328.15 |
0.9548 |
995.78 |
328.15 |
0.9556 |
995.62 |
328.15 |
0.9602 |
994.7 |
328.15 |
0.9700 |
992.65 |
328.15 |
0.9801 |
990.44 |
328.15 |
0.9897 |
988.21 |
328.15 |
0.9921 |
987.63 |
328.15 |
0.9951 |
986.91 |
338.15 |
0.0622 |
1024.56 |
338.15 |
0.1496 |
1024.59 |
338.15 |
0.2563 |
1024.49 |
338.15 |
0.3500 |
1024.2 |
338.15 |
0.4555 |
1023.41 |
338.15 |
0.5000 |
1022.84 |
338.15 |
0.5548 |
1021.85 |
338.15 |
0.6522 |
1019.0 |
338.15 |
0.7553 |
1013.69 |
338.15 |
0.8522 |
1005.25 |
338.15 |
0.9085 |
998.04 |
338.15 |
0.9147 |
997.1 |
338.15 |
0.9255 |
995.41 |
338.15 |
0.9350 |
993.83 |
338.15 |
0.9548 |
990.28 |
338.15 |
0.9556 |
990.13 |
338.15 |
0.9602 |
989.24 |
338.15 |
0.9700 |
987.28 |
338.15 |
0.9801 |
985.14 |
338.15 |
0.9897 |
982.99 |
338.15 |
0.9921 |
982.43 |
338.15 |
0.9951 |
981.73 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Frequency, MHz = 3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Speed of sound, m/s - Liquid |
283.15 |
0.0000 |
1659.5 |
283.15 |
0.1022 |
1672.9 |
283.15 |
0.2010 |
1686.6 |
283.15 |
0.2987 |
1702.0 |
283.15 |
0.3998 |
1717.3 |
283.15 |
0.4997 |
1732.0 |
283.15 |
0.5997 |
1742.7 |
283.15 |
0.6999 |
1742.0 |
283.15 |
0.7999 |
1718.2 |
283.15 |
0.8997 |
1637.8 |
283.15 |
1.0000 |
1448.1 |
293.15 |
0.0000 |
1636.3 |
293.15 |
0.1022 |
1650.1 |
293.15 |
0.2010 |
1664.0 |
293.15 |
0.2987 |
1679.4 |
293.15 |
0.3998 |
1695.2 |
293.15 |
0.4997 |
1710.5 |
293.15 |
0.5997 |
1722.7 |
293.15 |
0.6999 |
1725.1 |
293.15 |
0.7999 |
1707.4 |
293.15 |
0.8997 |
1641.2 |
293.15 |
1.0000 |
1482.7 |
303.15 |
0.0000 |
1613.6 |
303.15 |
0.1022 |
1627.2 |
303.15 |
0.2010 |
1641.4 |
303.15 |
0.2987 |
1656.8 |
303.15 |
0.3998 |
1672.8 |
303.15 |
0.4997 |
1688.7 |
303.15 |
0.5997 |
1701.9 |
303.15 |
0.6999 |
1707.1 |
303.15 |
0.7999 |
1695.0 |
303.15 |
0.8997 |
1641.6 |
303.15 |
1.0000 |
1509.4 |
313.15 |
0.0000 |
1591.1 |
313.15 |
0.1022 |
1605.0 |
313.15 |
0.2010 |
1618.9 |
313.15 |
0.2987 |
1634.1 |
313.15 |
0.3998 |
1650.2 |
313.15 |
0.4997 |
1666.4 |
313.15 |
0.5997 |
1680.5 |
313.15 |
0.6999 |
1688.1 |
313.15 |
0.7999 |
1680.9 |
313.15 |
0.8997 |
1639.0 |
313.15 |
1.0000 |
1529.2 |
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 |
0.0622 |
1650.1 |
298.15 |
0.1496 |
1654.3 |
298.15 |
0.2563 |
1670.2 |
298.15 |
0.3500 |
1693.5 |
298.15 |
0.4555 |
1717.8 |
298.15 |
0.5000 |
1723.1 |
298.15 |
0.5548 |
1726.1 |
298.15 |
0.6522 |
1723.3 |
298.15 |
0.7553 |
1712.1 |
298.15 |
0.8522 |
1689.1 |
298.15 |
0.9085 |
1653.2 |
298.15 |
0.9147 |
1646.8 |
298.15 |
0.9255 |
1636.1 |
298.15 |
0.9350 |
1623.9 |
298.15 |
0.9548 |
1596.0 |
298.15 |
0.9556 |
1594.0 |
298.15 |
0.9602 |
1586.0 |
298.15 |
0.9700 |
1568.2 |
298.15 |
0.9801 |
1547.1 |
298.15 |
0.9897 |
1525.3 |
298.15 |
0.9921 |
1519.1 |
298.15 |
0.9951 |
1511.0 |
308.15 |
0.0622 |
1627.1 |
308.15 |
0.1496 |
1634.1 |
308.15 |
0.2563 |
1645.9 |
308.15 |
0.3500 |
1662.2 |
308.15 |
0.4555 |
1681.0 |
308.15 |
0.5000 |
1688.0 |
308.15 |
0.5548 |
1695.1 |
308.15 |
0.6522 |
1702.2 |
308.15 |
0.7553 |
1698.8 |
308.15 |
0.8522 |
1676.1 |
308.15 |
0.9085 |
1642.1 |
308.15 |
0.9147 |
1637.1 |
308.15 |
0.9255 |
1627.1 |
308.15 |
0.9350 |
1617.2 |
308.15 |
0.9548 |
1594.1 |
308.15 |
0.9556 |
1593.1 |
308.15 |
0.9602 |
1586.2 |
308.15 |
0.9700 |
1572.1 |
308.15 |
0.9801 |
1556.1 |
308.15 |
0.9897 |
1539.3 |
308.15 |
0.9921 |
1534.1 |
308.15 |
0.9951 |
1528.8 |
318.15 |
0.0622 |
1609.1 |
318.15 |
0.1496 |
1616.0 |
318.15 |
0.2563 |
1627.8 |
318.15 |
0.3500 |
1643.0 |
318.15 |
0.4555 |
1661.0 |
318.15 |
0.5000 |
1667.0 |
318.15 |
0.5548 |
1674.1 |
318.15 |
0.6522 |
1682.0 |
318.15 |
0.7553 |
1683.0 |
318.15 |
0.8522 |
1666.1 |
318.15 |
0.9085 |
1639.2 |
318.15 |
0.9147 |
1635.3 |
318.15 |
0.9255 |
1625.9 |
318.15 |
0.9350 |
1617.9 |
318.15 |
0.9548 |
1598.1 |
318.15 |
0.9556 |
1592.2 |
318.15 |
0.9602 |
1580.1 |
318.15 |
0.9700 |
1566.1 |
318.15 |
0.9801 |
1552.1 |
318.15 |
0.9897 |
1549.9 |
318.15 |
0.9921 |
1548.1 |
318.15 |
0.9951 |
1543.2 |
328.15 |
0.0622 |
1585.1 |
328.15 |
0.1496 |
1591.1 |
328.15 |
0.2563 |
1603.2 |
328.15 |
0.3500 |
1618.2 |
328.15 |
0.4555 |
1635.8 |
328.15 |
0.5000 |
1642.1 |
328.15 |
0.5548 |
1649.1 |
328.15 |
0.6522 |
1657.8 |
328.15 |
0.7553 |
1661.1 |
328.15 |
0.8522 |
1651.2 |
328.15 |
0.9085 |
1630.0 |
328.15 |
0.9147 |
1626.2 |
328.15 |
0.9255 |
1620.2 |
328.15 |
0.9350 |
1613.2 |
328.15 |
0.9548 |
1597.2 |
328.15 |
0.9556 |
1596.1 |
328.15 |
0.9602 |
1591.8 |
328.15 |
0.9700 |
1582.1 |
328.15 |
0.9801 |
1571.1 |
328.15 |
0.9897 |
1559.2 |
328.15 |
0.9921 |
1556.2 |
328.15 |
0.9951 |
1552.2 |
338.15 |
0.0622 |
1565.1 |
338.15 |
0.1496 |
1571.2 |
338.15 |
0.2563 |
1582.3 |
338.15 |
0.3500 |
1594.8 |
338.15 |
0.4555 |
1611.1 |
338.15 |
0.5000 |
1616.8 |
338.15 |
0.5548 |
1623.9 |
338.15 |
0.6522 |
1634.1 |
338.15 |
0.7553 |
1639.0 |
338.15 |
0.8522 |
1632.0 |
338.15 |
0.9085 |
1616.0 |
338.15 |
0.9147 |
1613.2 |
338.15 |
0.9255 |
1608.2 |
338.15 |
0.9350 |
1603.1 |
338.15 |
0.9548 |
1591.1 |
338.15 |
0.9556 |
1591.3 |
338.15 |
0.9602 |
1587.1 |
338.15 |
0.9700 |
1579.9 |
338.15 |
0.9801 |
1571.0 |
338.15 |
0.9897 |
1562.0 |
338.15 |
0.9921 |
1559.1 |
338.15 |
0.9951 |
1556.0 |
Speed of sound, m/s
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Frequency, MHz = 3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (2) - Liquid |
Speed of sound, m/s - Liquid |
283.15 |
0.0000 |
1659.5 |
283.15 |
0.1022 |
1672.9 |
283.15 |
0.2010 |
1686.6 |
283.15 |
0.2987 |
1702.0 |
283.15 |
0.3998 |
1717.3 |
283.15 |
0.4997 |
1732.0 |
283.15 |
0.5997 |
1742.7 |
283.15 |
0.6999 |
1742.0 |
283.15 |
0.7999 |
1718.2 |
283.15 |
0.8997 |
1637.8 |
283.15 |
1.0000 |
1448.1 |
293.15 |
0.0000 |
1636.3 |
293.15 |
0.1022 |
1650.1 |
293.15 |
0.2010 |
1664.0 |
293.15 |
0.2987 |
1679.4 |
293.15 |
0.3998 |
1695.2 |
293.15 |
0.4997 |
1710.5 |
293.15 |
0.5997 |
1722.7 |
293.15 |
0.6999 |
1725.1 |
293.15 |
0.7999 |
1707.4 |
293.15 |
0.8997 |
1641.2 |
293.15 |
1.0000 |
1482.7 |
303.15 |
0.0000 |
1613.6 |
303.15 |
0.1022 |
1627.2 |
303.15 |
0.2010 |
1641.4 |
303.15 |
0.2987 |
1656.8 |
303.15 |
0.3998 |
1672.8 |
303.15 |
0.4997 |
1688.7 |
303.15 |
0.5997 |
1701.9 |
303.15 |
0.6999 |
1707.1 |
303.15 |
0.7999 |
1695.0 |
303.15 |
0.8997 |
1641.6 |
303.15 |
1.0000 |
1509.4 |
313.15 |
0.0000 |
1591.1 |
313.15 |
0.1022 |
1605.0 |
313.15 |
0.2010 |
1618.9 |
313.15 |
0.2987 |
1634.1 |
313.15 |
0.3998 |
1650.2 |
313.15 |
0.4997 |
1666.4 |
313.15 |
0.5997 |
1680.5 |
313.15 |
0.6999 |
1688.1 |
313.15 |
0.7999 |
1680.9 |
313.15 |
0.8997 |
1639.0 |
313.15 |
1.0000 |
1529.2 |
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 |
0.0622 |
1650.1 |
298.15 |
0.1496 |
1654.3 |
298.15 |
0.2563 |
1670.2 |
298.15 |
0.3500 |
1693.5 |
298.15 |
0.4555 |
1717.8 |
298.15 |
0.5000 |
1723.1 |
298.15 |
0.5548 |
1726.1 |
298.15 |
0.6522 |
1723.3 |
298.15 |
0.7553 |
1712.1 |
298.15 |
0.8522 |
1689.1 |
298.15 |
0.9085 |
1653.2 |
298.15 |
0.9147 |
1646.8 |
298.15 |
0.9255 |
1636.1 |
298.15 |
0.9350 |
1623.9 |
298.15 |
0.9548 |
1596.0 |
298.15 |
0.9556 |
1594.0 |
298.15 |
0.9602 |
1586.0 |
298.15 |
0.9700 |
1568.2 |
298.15 |
0.9801 |
1547.1 |
298.15 |
0.9897 |
1525.3 |
298.15 |
0.9921 |
1519.1 |
298.15 |
0.9951 |
1511.0 |
308.15 |
0.0622 |
1627.1 |
308.15 |
0.1496 |
1634.1 |
308.15 |
0.2563 |
1645.9 |
308.15 |
0.3500 |
1662.2 |
308.15 |
0.4555 |
1681.0 |
308.15 |
0.5000 |
1688.0 |
308.15 |
0.5548 |
1695.1 |
308.15 |
0.6522 |
1702.2 |
308.15 |
0.7553 |
1698.8 |
308.15 |
0.8522 |
1676.1 |
308.15 |
0.9085 |
1642.1 |
308.15 |
0.9147 |
1637.1 |
308.15 |
0.9255 |
1627.1 |
308.15 |
0.9350 |
1617.2 |
308.15 |
0.9548 |
1594.1 |
308.15 |
0.9556 |
1593.1 |
308.15 |
0.9602 |
1586.2 |
308.15 |
0.9700 |
1572.1 |
308.15 |
0.9801 |
1556.1 |
308.15 |
0.9897 |
1539.3 |
308.15 |
0.9921 |
1534.1 |
308.15 |
0.9951 |
1528.8 |
318.15 |
0.0622 |
1609.1 |
318.15 |
0.1496 |
1616.0 |
318.15 |
0.2563 |
1627.8 |
318.15 |
0.3500 |
1643.0 |
318.15 |
0.4555 |
1661.0 |
318.15 |
0.5000 |
1667.0 |
318.15 |
0.5548 |
1674.1 |
318.15 |
0.6522 |
1682.0 |
318.15 |
0.7553 |
1683.0 |
318.15 |
0.8522 |
1666.1 |
318.15 |
0.9085 |
1639.2 |
318.15 |
0.9147 |
1635.3 |
318.15 |
0.9255 |
1625.9 |
318.15 |
0.9350 |
1617.9 |
318.15 |
0.9548 |
1598.1 |
318.15 |
0.9556 |
1592.2 |
318.15 |
0.9602 |
1580.1 |
318.15 |
0.9700 |
1566.1 |
318.15 |
0.9801 |
1552.1 |
318.15 |
0.9897 |
1549.9 |
318.15 |
0.9921 |
1548.1 |
318.15 |
0.9951 |
1543.2 |
328.15 |
0.0622 |
1585.1 |
328.15 |
0.1496 |
1591.1 |
328.15 |
0.2563 |
1603.2 |
328.15 |
0.3500 |
1618.2 |
328.15 |
0.4555 |
1635.8 |
328.15 |
0.5000 |
1642.1 |
328.15 |
0.5548 |
1649.1 |
328.15 |
0.6522 |
1657.8 |
328.15 |
0.7553 |
1661.1 |
328.15 |
0.8522 |
1651.2 |
328.15 |
0.9085 |
1630.0 |
328.15 |
0.9147 |
1626.2 |
328.15 |
0.9255 |
1620.2 |
328.15 |
0.9350 |
1613.2 |
328.15 |
0.9548 |
1597.2 |
328.15 |
0.9556 |
1596.1 |
328.15 |
0.9602 |
1591.8 |
328.15 |
0.9700 |
1582.1 |
328.15 |
0.9801 |
1571.1 |
328.15 |
0.9897 |
1559.2 |
328.15 |
0.9921 |
1556.2 |
328.15 |
0.9951 |
1552.2 |
338.15 |
0.0622 |
1565.1 |
338.15 |
0.1496 |
1571.2 |
338.15 |
0.2563 |
1582.3 |
338.15 |
0.3500 |
1594.8 |
338.15 |
0.4555 |
1611.1 |
338.15 |
0.5000 |
1616.8 |
338.15 |
0.5548 |
1623.9 |
338.15 |
0.6522 |
1634.1 |
338.15 |
0.7553 |
1639.0 |
338.15 |
0.8522 |
1632.0 |
338.15 |
0.9085 |
1616.0 |
338.15 |
0.9147 |
1613.2 |
338.15 |
0.9255 |
1608.2 |
338.15 |
0.9350 |
1603.1 |
338.15 |
0.9548 |
1591.1 |
338.15 |
0.9556 |
1591.3 |
338.15 |
0.9602 |
1587.1 |
338.15 |
0.9700 |
1579.9 |
338.15 |
0.9801 |
1571.0 |
338.15 |
0.9897 |
1562.0 |
338.15 |
0.9921 |
1559.1 |
338.15 |
0.9951 |
1556.0 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Water (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0780 |
446.27 |
0.1750 |
421.88 |
0.2470 |
411.12 |
0.3410 |
401.20 |
0.4020 |
396.38 |
0.4590 |
392.63 |
0.5270 |
388.89 |
0.5710 |
386.85 |
0.6330 |
384.18 |
0.6820 |
382.36 |
0.7330 |
380.81 |
0.7780 |
379.38 |
0.8210 |
378.22 |
0.8800 |
376.45 |
0.9320 |
375.04 |
0.9800 |
373.76 |
1.0000 |
373.15 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Water (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0780 |
446.27 |
0.1750 |
421.88 |
0.2470 |
411.12 |
0.3410 |
401.20 |
0.4020 |
396.38 |
0.4590 |
392.63 |
0.5270 |
388.89 |
0.5710 |
386.85 |
0.6330 |
384.18 |
0.6820 |
382.36 |
0.7330 |
380.81 |
0.7780 |
379.38 |
0.8210 |
378.22 |
0.8800 |
376.45 |
0.9320 |
375.04 |
0.9800 |
373.76 |
1.0000 |
373.15 |
Excess molar volume, m3/mol
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,3-Propanediol (1) - Liquid |
Excess molar volume, m3/mol - Liquid |
283.15 |
0.0248 |
-2.2300e-08 |
283.15 |
0.0369 |
-4.0800e-08 |
283.15 |
0.0502 |
-6.4200e-08 |
283.15 |
0.0751 |
-1.1540e-07 |
283.15 |
0.0803 |
-1.2680e-07 |
283.15 |
0.0993 |
-1.6780e-07 |
283.15 |
0.1401 |
-2.4720e-07 |
283.15 |
0.1504 |
-2.6510e-07 |
283.15 |
0.1987 |
-3.4260e-07 |
283.15 |
0.2990 |
-4.4170e-07 |
283.15 |
0.3982 |
-4.7680e-07 |
283.15 |
0.4976 |
-4.6290e-07 |
283.15 |
0.5952 |
-4.1390e-07 |
283.15 |
0.5955 |
-4.1290e-07 |
283.15 |
0.7025 |
-3.2840e-07 |
283.15 |
0.7902 |
-2.4130e-07 |
283.15 |
0.8989 |
-1.1930e-07 |
283.15 |
0.9455 |
-6.6600e-08 |
293.15 |
0.0248 |
-2.2200e-08 |
293.15 |
0.0369 |
-3.9500e-08 |
293.15 |
0.0502 |
-6.0700e-08 |
293.15 |
0.0751 |
-1.0630e-07 |
293.15 |
0.0803 |
-1.1650e-07 |
293.15 |
0.0993 |
-1.5290e-07 |
293.15 |
0.1401 |
-2.2410e-07 |
293.15 |
0.1504 |
-2.4030e-07 |
293.15 |
0.1987 |
-3.1130e-07 |
293.15 |
0.2990 |
-4.0460e-07 |
293.15 |
0.3982 |
-4.4010e-07 |
293.15 |
0.4976 |
-4.2990e-07 |
293.15 |
0.5952 |
-3.8610e-07 |
293.15 |
0.5955 |
-3.8560e-07 |
293.15 |
0.7025 |
-3.0780e-07 |
293.15 |
0.7902 |
-2.2690e-07 |
293.15 |
0.8989 |
-1.1210e-07 |
293.15 |
0.9455 |
-6.2700e-08 |
298.15 |
0.0248 |
-2.2200e-08 |
298.15 |
0.0369 |
-3.9000e-08 |
298.15 |
0.0502 |
-5.9400e-08 |
298.15 |
0.0751 |
-1.0290e-07 |
298.15 |
0.0803 |
-1.1250e-07 |
298.15 |
0.0993 |
-1.4720e-07 |
298.15 |
0.1401 |
-2.1490e-07 |
298.15 |
0.1504 |
-2.3040e-07 |
298.15 |
0.1987 |
-2.9840e-07 |
298.15 |
0.2990 |
-3.8870e-07 |
298.15 |
0.3982 |
-4.2410e-07 |
298.15 |
0.4976 |
-4.1540e-07 |
298.15 |
0.5952 |
-3.7410e-07 |
298.15 |
0.5955 |
-3.7380e-07 |
298.15 |
0.7025 |
-2.9900e-07 |
298.15 |
0.7902 |
-2.2100e-07 |
298.15 |
0.8989 |
-1.0970e-07 |
298.15 |
0.9455 |
-6.1500e-08 |
303.15 |
0.0248 |
-2.2100e-08 |
303.15 |
0.0369 |
-3.8500e-08 |
303.15 |
0.0502 |
-5.8300e-08 |
303.15 |
0.0751 |
-9.9800e-08 |
303.15 |
0.0803 |
-1.0910e-07 |
303.15 |
0.0993 |
-1.4210e-07 |
303.15 |
0.1401 |
-2.0650e-07 |
303.15 |
0.1504 |
-2.2130e-07 |
303.15 |
0.1987 |
-2.8650e-07 |
303.15 |
0.2990 |
-3.7410e-07 |
303.15 |
0.3982 |
-4.0920e-07 |
303.15 |
0.4976 |
-4.0180e-07 |
303.15 |
0.5952 |
-3.6280e-07 |
303.15 |
0.5955 |
-3.6250e-07 |
303.15 |
0.7025 |
-2.9070e-07 |
303.15 |
0.7902 |
-2.1520e-07 |
303.15 |
0.8989 |
-1.0680e-07 |
303.15 |
0.9455 |
-5.9900e-08 |
313.15 |
0.0248 |
-2.1600e-08 |
313.15 |
0.0369 |
-3.7000e-08 |
313.15 |
0.0502 |
-5.6000e-08 |
313.15 |
0.0751 |
-9.4300e-08 |
313.15 |
0.0803 |
-1.0270e-07 |
313.15 |
0.0993 |
-1.3290e-07 |
313.15 |
0.1401 |
-1.9170e-07 |
313.15 |
0.1504 |
-2.0520e-07 |
313.15 |
0.1987 |
-2.6530e-07 |
313.15 |
0.2990 |
-3.4730e-07 |
313.15 |
0.3982 |
-3.8170e-07 |
313.15 |
0.4976 |
-3.7670e-07 |
313.15 |
0.5952 |
-3.4150e-07 |
313.15 |
0.5955 |
-3.4140e-07 |
313.15 |
0.7025 |
-2.7510e-07 |
313.15 |
0.7902 |
-2.0410e-07 |
313.15 |
0.8989 |
-1.0170e-07 |
313.15 |
0.9455 |
-5.7200e-08 |
Partial molar volume, m3/mol of 1,3-Propanediol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Partial molar volume, m3/mol of 1,3-Propanediol (1) - Liquid |
298.22 |
640.00 |
0.0001 |
298.22 |
29780.00 |
0.0001 |
298.23 |
15160.00 |
0.0001 |
318.17 |
480.00 |
0.0001 |
318.17 |
14770.00 |
0.0001 |
318.17 |
30240.00 |
0.0001 |
338.16 |
440.00 |
0.0001 |
338.16 |
15130.00 |
0.0001 |
338.16 |
30290.00 |
0.0001 |
373.13 |
30110.00 |
0.0001 |
373.14 |
15170.00 |
0.0001 |
373.16 |
1960.00 |
0.0001 |
408.15 |
14940.00 |
0.0001 |
408.15 |
30010.00 |
0.0001 |
408.16 |
1870.00 |
0.0001 |
442.02 |
1820.00 |
0.0001 |
442.03 |
15700.00 |
0.0001 |
442.08 |
29800.00 |
0.0001 |
473.15 |
1940.00 |
0.0001 |
473.16 |
15710.00 |
0.0001 |
473.16 |
30280.00 |
0.0001 |
498.15 |
15940.00 |
0.0001 |
498.16 |
2960.00 |
0.0001 |
498.16 |
30110.00 |
0.0001 |
523.16 |
5030.00 |
0.0001 |
523.16 |
16160.00 |
0.0001 |
523.16 |
30260.00 |
0.0001 |
548.18 |
7070.00 |
0.0001 |
548.18 |
18040.00 |
0.0001 |
548.18 |
30580.00 |
0.0001 |
573.17 |
30240.00 |
0.0001 |
573.18 |
10100.00 |
0.0001 |
573.19 |
19920.00 |
0.0001 |
Excess molar volume, m3/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of 1,3-Propanediol (1) - Liquid |
Excess molar volume, m3/mol - Liquid |
0.0731 |
-9.9800e-08 |
0.1555 |
-2.1580e-07 |
0.2449 |
-3.2740e-07 |
0.3384 |
-4.0080e-07 |
0.4321 |
-4.2710e-07 |
0.5223 |
-4.1180e-07 |
0.6058 |
-3.6530e-07 |
0.6803 |
-3.0780e-07 |
0.7446 |
-2.5490e-07 |
0.7987 |
-2.0690e-07 |
0.8430 |
-1.6600e-07 |
0.8786 |
-1.3140e-07 |
0.9068 |
-1.0670e-07 |
0.9355 |
-7.5200e-08 |
Excess molar volume, m3/mol
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of 1,3-Propanediol (1) - Liquid |
Excess molar volume, m3/mol - Liquid |
283.15 |
0.0248 |
-2.2300e-08 |
283.15 |
0.0369 |
-4.0800e-08 |
283.15 |
0.0502 |
-6.4200e-08 |
283.15 |
0.0751 |
-1.1540e-07 |
283.15 |
0.0803 |
-1.2680e-07 |
283.15 |
0.0993 |
-1.6780e-07 |
283.15 |
0.1401 |
-2.4720e-07 |
283.15 |
0.1504 |
-2.6510e-07 |
283.15 |
0.1987 |
-3.4260e-07 |
283.15 |
0.2990 |
-4.4170e-07 |
283.15 |
0.3982 |
-4.7680e-07 |
283.15 |
0.4976 |
-4.6290e-07 |
283.15 |
0.5952 |
-4.1390e-07 |
283.15 |
0.5955 |
-4.1290e-07 |
283.15 |
0.7025 |
-3.2840e-07 |
283.15 |
0.7902 |
-2.4130e-07 |
283.15 |
0.8989 |
-1.1930e-07 |
283.15 |
0.9455 |
-6.6600e-08 |
293.15 |
0.0248 |
-2.2200e-08 |
293.15 |
0.0369 |
-3.9500e-08 |
293.15 |
0.0502 |
-6.0700e-08 |
293.15 |
0.0751 |
-1.0630e-07 |
293.15 |
0.0803 |
-1.1650e-07 |
293.15 |
0.0993 |
-1.5290e-07 |
293.15 |
0.1401 |
-2.2410e-07 |
293.15 |
0.1504 |
-2.4030e-07 |
293.15 |
0.1987 |
-3.1130e-07 |
293.15 |
0.2990 |
-4.0460e-07 |
293.15 |
0.3982 |
-4.4010e-07 |
293.15 |
0.4976 |
-4.2990e-07 |
293.15 |
0.5952 |
-3.8610e-07 |
293.15 |
0.5955 |
-3.8560e-07 |
293.15 |
0.7025 |
-3.0780e-07 |
293.15 |
0.7902 |
-2.2690e-07 |
293.15 |
0.8989 |
-1.1210e-07 |
293.15 |
0.9455 |
-6.2700e-08 |
298.15 |
0.0248 |
-2.2200e-08 |
298.15 |
0.0369 |
-3.9000e-08 |
298.15 |
0.0502 |
-5.9400e-08 |
298.15 |
0.0751 |
-1.0290e-07 |
298.15 |
0.0803 |
-1.1250e-07 |
298.15 |
0.0993 |
-1.4720e-07 |
298.15 |
0.1401 |
-2.1490e-07 |
298.15 |
0.1504 |
-2.3040e-07 |
298.15 |
0.1987 |
-2.9840e-07 |
298.15 |
0.2990 |
-3.8870e-07 |
298.15 |
0.3982 |
-4.2410e-07 |
298.15 |
0.4976 |
-4.1540e-07 |
298.15 |
0.5952 |
-3.7410e-07 |
298.15 |
0.5955 |
-3.7380e-07 |
298.15 |
0.7025 |
-2.9900e-07 |
298.15 |
0.7902 |
-2.2100e-07 |
298.15 |
0.8989 |
-1.0970e-07 |
298.15 |
0.9455 |
-6.1500e-08 |
303.15 |
0.0248 |
-2.2100e-08 |
303.15 |
0.0369 |
-3.8500e-08 |
303.15 |
0.0502 |
-5.8300e-08 |
303.15 |
0.0751 |
-9.9800e-08 |
303.15 |
0.0803 |
-1.0910e-07 |
303.15 |
0.0993 |
-1.4210e-07 |
303.15 |
0.1401 |
-2.0650e-07 |
303.15 |
0.1504 |
-2.2130e-07 |
303.15 |
0.1987 |
-2.8650e-07 |
303.15 |
0.2990 |
-3.7410e-07 |
303.15 |
0.3982 |
-4.0920e-07 |
303.15 |
0.4976 |
-4.0180e-07 |
303.15 |
0.5952 |
-3.6280e-07 |
303.15 |
0.5955 |
-3.6250e-07 |
303.15 |
0.7025 |
-2.9070e-07 |
303.15 |
0.7902 |
-2.1520e-07 |
303.15 |
0.8989 |
-1.0680e-07 |
303.15 |
0.9455 |
-5.9900e-08 |
313.15 |
0.0248 |
-2.1600e-08 |
313.15 |
0.0369 |
-3.7000e-08 |
313.15 |
0.0502 |
-5.6000e-08 |
313.15 |
0.0751 |
-9.4300e-08 |
313.15 |
0.0803 |
-1.0270e-07 |
313.15 |
0.0993 |
-1.3290e-07 |
313.15 |
0.1401 |
-1.9170e-07 |
313.15 |
0.1504 |
-2.0520e-07 |
313.15 |
0.1987 |
-2.6530e-07 |
313.15 |
0.2990 |
-3.4730e-07 |
313.15 |
0.3982 |
-3.8170e-07 |
313.15 |
0.4976 |
-3.7670e-07 |
313.15 |
0.5952 |
-3.4150e-07 |
313.15 |
0.5955 |
-3.4140e-07 |
313.15 |
0.7025 |
-2.7510e-07 |
313.15 |
0.7902 |
-2.0410e-07 |
313.15 |
0.8989 |
-1.0170e-07 |
313.15 |
0.9455 |
-5.7200e-08 |
Partial molar volume, m3/mol of 1,3-Propanediol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Partial molar volume, m3/mol of 1,3-Propanediol (1) - Liquid |
298.22 |
640.00 |
0.0001 |
298.22 |
29780.00 |
0.0001 |
298.23 |
15160.00 |
0.0001 |
318.17 |
480.00 |
0.0001 |
318.17 |
14770.00 |
0.0001 |
318.17 |
30240.00 |
0.0001 |
338.16 |
440.00 |
0.0001 |
338.16 |
15130.00 |
0.0001 |
338.16 |
30290.00 |
0.0001 |
373.13 |
30110.00 |
0.0001 |
373.14 |
15170.00 |
0.0001 |
373.16 |
1960.00 |
0.0001 |
408.15 |
14940.00 |
0.0001 |
408.15 |
30010.00 |
0.0001 |
408.16 |
1870.00 |
0.0001 |
442.02 |
1820.00 |
0.0001 |
442.03 |
15700.00 |
0.0001 |
442.08 |
29800.00 |
0.0001 |
473.15 |
1940.00 |
0.0001 |
473.16 |
15710.00 |
0.0001 |
473.16 |
30280.00 |
0.0001 |
498.15 |
15940.00 |
0.0001 |
498.16 |
2960.00 |
0.0001 |
498.16 |
30110.00 |
0.0001 |
523.16 |
5030.00 |
0.0001 |
523.16 |
16160.00 |
0.0001 |
523.16 |
30260.00 |
0.0001 |
548.18 |
7070.00 |
0.0001 |
548.18 |
18040.00 |
0.0001 |
548.18 |
30580.00 |
0.0001 |
573.17 |
30240.00 |
0.0001 |
573.18 |
10100.00 |
0.0001 |
573.19 |
19920.00 |
0.0001 |
Excess molar volume, m3/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of 1,3-Propanediol (1) - Liquid |
Excess molar volume, m3/mol - Liquid |
0.0731 |
-9.9800e-08 |
0.1555 |
-2.1580e-07 |
0.2449 |
-3.2740e-07 |
0.3384 |
-4.0080e-07 |
0.4321 |
-4.2710e-07 |
0.5223 |
-4.1180e-07 |
0.6058 |
-3.6530e-07 |
0.6803 |
-3.0780e-07 |
0.7446 |
-2.5490e-07 |
0.7987 |
-2.0690e-07 |
0.8430 |
-1.6600e-07 |
0.8786 |
-1.3140e-07 |
0.9068 |
-1.0670e-07 |
0.9355 |
-7.5200e-08 |
Sources
-
Excess volumes and excess heat capacities for alkanediol + water systems in the temperature interval (283.15-313.15) K
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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
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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
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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
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Isobaric (vapor + liquid) equilibria for the ternary system of (ethanol + water + 1,3-propanediol) and three constituent binary systems at P = 101.3 kPa
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Vapor-liquid equilibria, density and sound velocity measurements of (water or methanol or ethanol + 1,3-propanediol) binary systems at different temperatures
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Viscosities, Densities, and Refractive Indices of Aqueous Propane-1,3-diol
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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
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Enthalpies of Dilution of 1,3-Propanediol and Isomers of 2,3-Butanediol in Dimethylsulfoxide + Water Mixtures at 298.15 K