Datasets
-
η - Viscosity, Pa*s (6)
-
n0 - Refractive index (Na D-line) (4)
-
ρl - Mass density, kg/m3 (8)
-
csound,fluid - Speed of Sound, m/s (2)
Viscosity, Pa*s
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Viscosity, Pa*s - Liquid |
303.15 |
101.30 |
0.0800 |
0.0011 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0000 |
0.0010 |
293.15 |
0.0122 |
0.0015 |
293.15 |
0.0271 |
0.0023 |
293.15 |
0.0454 |
0.0032 |
293.15 |
0.0689 |
0.0043 |
293.15 |
0.0998 |
0.0056 |
293.15 |
0.1428 |
0.0068 |
293.15 |
0.2062 |
0.0079 |
293.15 |
0.3078 |
0.0084 |
293.15 |
0.4037 |
0.0082 |
293.15 |
0.5015 |
0.0078 |
293.15 |
0.6107 |
0.0073 |
293.15 |
0.7050 |
0.0069 |
293.15 |
0.7958 |
0.0066 |
293.15 |
0.8932 |
0.0062 |
293.15 |
1.0000 |
0.0058 |
303.15 |
0.0000 |
0.0008 |
303.15 |
0.0122 |
0.0011 |
303.15 |
0.0271 |
0.0016 |
303.15 |
0.0454 |
0.0023 |
303.15 |
0.0689 |
0.0031 |
303.15 |
0.0998 |
0.0039 |
303.15 |
0.1428 |
0.0047 |
303.15 |
0.2062 |
0.0054 |
303.15 |
0.3078 |
0.0058 |
303.15 |
0.4037 |
0.0057 |
303.15 |
0.5015 |
0.0056 |
303.15 |
0.6107 |
0.0053 |
303.15 |
0.7050 |
0.0050 |
303.15 |
0.7958 |
0.0048 |
303.15 |
0.8932 |
0.0045 |
303.15 |
1.0000 |
0.0042 |
313.15 |
0.0000 |
0.0007 |
313.15 |
0.0122 |
0.0009 |
313.15 |
0.0271 |
0.0013 |
313.15 |
0.0454 |
0.0018 |
313.15 |
0.0689 |
0.0023 |
313.15 |
0.0998 |
0.0029 |
313.15 |
0.1428 |
0.0034 |
313.15 |
0.2062 |
0.0039 |
313.15 |
0.3078 |
0.0042 |
313.15 |
0.4037 |
0.0042 |
313.15 |
0.5015 |
0.0040 |
313.15 |
0.6107 |
0.0039 |
313.15 |
0.7050 |
0.0037 |
313.15 |
0.7958 |
0.0035 |
313.15 |
0.8932 |
0.0034 |
313.15 |
1.0000 |
0.0032 |
323.15 |
0.0000 |
0.0005 |
323.15 |
0.0122 |
0.0007 |
323.15 |
0.0271 |
0.0010 |
323.15 |
0.0454 |
0.0014 |
323.15 |
0.0689 |
0.0018 |
323.15 |
0.0998 |
0.0022 |
323.15 |
0.1428 |
0.0026 |
323.15 |
0.2062 |
0.0029 |
323.15 |
0.3078 |
0.0031 |
323.15 |
0.4037 |
0.0031 |
323.15 |
0.5015 |
0.0030 |
323.15 |
0.6107 |
0.0029 |
323.15 |
0.7050 |
0.0028 |
323.15 |
0.7958 |
0.0027 |
323.15 |
0.8932 |
0.0026 |
323.15 |
1.0000 |
0.0025 |
333.15 |
0.0000 |
0.0005 |
333.15 |
0.0122 |
0.0006 |
333.15 |
0.0271 |
0.0008 |
333.15 |
0.0454 |
0.0011 |
333.15 |
0.0689 |
0.0014 |
333.15 |
0.0998 |
0.0017 |
333.15 |
0.1428 |
0.0020 |
333.15 |
0.2062 |
0.0022 |
333.15 |
0.3078 |
0.0024 |
333.15 |
0.4037 |
0.0024 |
333.15 |
0.5015 |
0.0023 |
333.15 |
0.6107 |
0.0023 |
333.15 |
0.7050 |
0.0022 |
333.15 |
0.7958 |
0.0021 |
333.15 |
0.8932 |
0.0021 |
333.15 |
1.0000 |
0.0020 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Viscosity, Pa*s - Liquid |
283.15 |
0.0000 |
0.0013 |
283.15 |
0.1000 |
0.0086 |
283.15 |
0.2000 |
0.0124 |
283.15 |
0.2999 |
0.0133 |
283.15 |
0.4000 |
0.0131 |
283.15 |
0.5000 |
0.0124 |
283.15 |
0.6000 |
0.0115 |
283.15 |
0.7000 |
0.0106 |
283.15 |
0.7998 |
0.0097 |
283.15 |
0.8999 |
0.0090 |
283.15 |
1.0000 |
0.0083 |
293.15 |
0.0000 |
0.0010 |
293.15 |
0.1000 |
0.0057 |
293.15 |
0.2000 |
0.0080 |
293.15 |
0.2999 |
0.0086 |
293.15 |
0.4000 |
0.0086 |
293.15 |
0.5000 |
0.0082 |
293.15 |
0.6000 |
0.0077 |
293.15 |
0.7000 |
0.0072 |
293.15 |
0.7998 |
0.0067 |
293.15 |
0.8999 |
0.0063 |
293.15 |
1.0000 |
0.0059 |
303.15 |
0.0000 |
0.0008 |
303.15 |
0.1000 |
0.0040 |
303.15 |
0.2000 |
0.0055 |
303.15 |
0.2999 |
0.0059 |
303.15 |
0.4000 |
0.0059 |
303.15 |
0.5000 |
0.0057 |
303.15 |
0.6000 |
0.0054 |
303.15 |
0.7000 |
0.0051 |
303.15 |
0.7998 |
0.0049 |
303.15 |
0.8999 |
0.0046 |
303.15 |
1.0000 |
0.0043 |
313.15 |
0.0000 |
0.0007 |
313.15 |
0.1000 |
0.0029 |
313.15 |
0.2000 |
0.0039 |
313.15 |
0.2999 |
0.0043 |
313.15 |
0.4000 |
0.0043 |
313.15 |
0.5000 |
0.0042 |
313.15 |
0.6000 |
0.0040 |
313.15 |
0.7000 |
0.0038 |
313.15 |
0.7998 |
0.0036 |
313.15 |
0.8999 |
0.0035 |
313.15 |
1.0000 |
0.0033 |
323.15 |
0.0000 |
0.0005 |
323.15 |
0.1000 |
0.0022 |
323.15 |
0.2000 |
0.0029 |
323.15 |
0.2999 |
0.0032 |
323.15 |
0.4000 |
0.0032 |
323.15 |
0.5000 |
0.0031 |
323.15 |
0.6000 |
0.0030 |
323.15 |
0.7000 |
0.0029 |
323.15 |
0.7998 |
0.0028 |
323.15 |
0.8999 |
0.0027 |
323.15 |
1.0000 |
0.0026 |
Viscosity, Pa*s
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Viscosity, Pa*s - Liquid |
303.15 |
101.30 |
0.0800 |
0.0011 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0000 |
0.0010 |
293.15 |
0.0122 |
0.0015 |
293.15 |
0.0271 |
0.0023 |
293.15 |
0.0454 |
0.0032 |
293.15 |
0.0689 |
0.0043 |
293.15 |
0.0998 |
0.0056 |
293.15 |
0.1428 |
0.0068 |
293.15 |
0.2062 |
0.0079 |
293.15 |
0.3078 |
0.0084 |
293.15 |
0.4037 |
0.0082 |
293.15 |
0.5015 |
0.0078 |
293.15 |
0.6107 |
0.0073 |
293.15 |
0.7050 |
0.0069 |
293.15 |
0.7958 |
0.0066 |
293.15 |
0.8932 |
0.0062 |
293.15 |
1.0000 |
0.0058 |
303.15 |
0.0000 |
0.0008 |
303.15 |
0.0122 |
0.0011 |
303.15 |
0.0271 |
0.0016 |
303.15 |
0.0454 |
0.0023 |
303.15 |
0.0689 |
0.0031 |
303.15 |
0.0998 |
0.0039 |
303.15 |
0.1428 |
0.0047 |
303.15 |
0.2062 |
0.0054 |
303.15 |
0.3078 |
0.0058 |
303.15 |
0.4037 |
0.0057 |
303.15 |
0.5015 |
0.0056 |
303.15 |
0.6107 |
0.0053 |
303.15 |
0.7050 |
0.0050 |
303.15 |
0.7958 |
0.0048 |
303.15 |
0.8932 |
0.0045 |
303.15 |
1.0000 |
0.0042 |
313.15 |
0.0000 |
0.0007 |
313.15 |
0.0122 |
0.0009 |
313.15 |
0.0271 |
0.0013 |
313.15 |
0.0454 |
0.0018 |
313.15 |
0.0689 |
0.0023 |
313.15 |
0.0998 |
0.0029 |
313.15 |
0.1428 |
0.0034 |
313.15 |
0.2062 |
0.0039 |
313.15 |
0.3078 |
0.0042 |
313.15 |
0.4037 |
0.0042 |
313.15 |
0.5015 |
0.0040 |
313.15 |
0.6107 |
0.0039 |
313.15 |
0.7050 |
0.0037 |
313.15 |
0.7958 |
0.0035 |
313.15 |
0.8932 |
0.0034 |
313.15 |
1.0000 |
0.0032 |
323.15 |
0.0000 |
0.0005 |
323.15 |
0.0122 |
0.0007 |
323.15 |
0.0271 |
0.0010 |
323.15 |
0.0454 |
0.0014 |
323.15 |
0.0689 |
0.0018 |
323.15 |
0.0998 |
0.0022 |
323.15 |
0.1428 |
0.0026 |
323.15 |
0.2062 |
0.0029 |
323.15 |
0.3078 |
0.0031 |
323.15 |
0.4037 |
0.0031 |
323.15 |
0.5015 |
0.0030 |
323.15 |
0.6107 |
0.0029 |
323.15 |
0.7050 |
0.0028 |
323.15 |
0.7958 |
0.0027 |
323.15 |
0.8932 |
0.0026 |
323.15 |
1.0000 |
0.0025 |
333.15 |
0.0000 |
0.0005 |
333.15 |
0.0122 |
0.0006 |
333.15 |
0.0271 |
0.0008 |
333.15 |
0.0454 |
0.0011 |
333.15 |
0.0689 |
0.0014 |
333.15 |
0.0998 |
0.0017 |
333.15 |
0.1428 |
0.0020 |
333.15 |
0.2062 |
0.0022 |
333.15 |
0.3078 |
0.0024 |
333.15 |
0.4037 |
0.0024 |
333.15 |
0.5015 |
0.0023 |
333.15 |
0.6107 |
0.0023 |
333.15 |
0.7050 |
0.0022 |
333.15 |
0.7958 |
0.0021 |
333.15 |
0.8932 |
0.0021 |
333.15 |
1.0000 |
0.0020 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Viscosity, Pa*s - Liquid |
283.15 |
0.0000 |
0.0013 |
283.15 |
0.1000 |
0.0086 |
283.15 |
0.2000 |
0.0124 |
283.15 |
0.2999 |
0.0133 |
283.15 |
0.4000 |
0.0131 |
283.15 |
0.5000 |
0.0124 |
283.15 |
0.6000 |
0.0115 |
283.15 |
0.7000 |
0.0106 |
283.15 |
0.7998 |
0.0097 |
283.15 |
0.8999 |
0.0090 |
283.15 |
1.0000 |
0.0083 |
293.15 |
0.0000 |
0.0010 |
293.15 |
0.1000 |
0.0057 |
293.15 |
0.2000 |
0.0080 |
293.15 |
0.2999 |
0.0086 |
293.15 |
0.4000 |
0.0086 |
293.15 |
0.5000 |
0.0082 |
293.15 |
0.6000 |
0.0077 |
293.15 |
0.7000 |
0.0072 |
293.15 |
0.7998 |
0.0067 |
293.15 |
0.8999 |
0.0063 |
293.15 |
1.0000 |
0.0059 |
303.15 |
0.0000 |
0.0008 |
303.15 |
0.1000 |
0.0040 |
303.15 |
0.2000 |
0.0055 |
303.15 |
0.2999 |
0.0059 |
303.15 |
0.4000 |
0.0059 |
303.15 |
0.5000 |
0.0057 |
303.15 |
0.6000 |
0.0054 |
303.15 |
0.7000 |
0.0051 |
303.15 |
0.7998 |
0.0049 |
303.15 |
0.8999 |
0.0046 |
303.15 |
1.0000 |
0.0043 |
313.15 |
0.0000 |
0.0007 |
313.15 |
0.1000 |
0.0029 |
313.15 |
0.2000 |
0.0039 |
313.15 |
0.2999 |
0.0043 |
313.15 |
0.4000 |
0.0043 |
313.15 |
0.5000 |
0.0042 |
313.15 |
0.6000 |
0.0040 |
313.15 |
0.7000 |
0.0038 |
313.15 |
0.7998 |
0.0036 |
313.15 |
0.8999 |
0.0035 |
313.15 |
1.0000 |
0.0033 |
323.15 |
0.0000 |
0.0005 |
323.15 |
0.1000 |
0.0022 |
323.15 |
0.2000 |
0.0029 |
323.15 |
0.2999 |
0.0032 |
323.15 |
0.4000 |
0.0032 |
323.15 |
0.5000 |
0.0031 |
323.15 |
0.6000 |
0.0030 |
323.15 |
0.7000 |
0.0029 |
323.15 |
0.7998 |
0.0028 |
323.15 |
0.8999 |
0.0027 |
323.15 |
1.0000 |
0.0026 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Refractive index (Na D-line) - Liquid |
283.15 |
0.0000 |
1.3337 |
283.15 |
0.1000 |
1.3916 |
283.15 |
0.2000 |
1.411 |
283.15 |
0.2999 |
1.4204 |
283.15 |
0.4000 |
1.4255 |
283.15 |
0.5000 |
1.4286 |
283.15 |
0.6000 |
1.4307 |
283.15 |
0.7000 |
1.4323 |
283.15 |
0.7998 |
1.4334 |
283.15 |
0.8999 |
1.4342 |
283.15 |
1.0000 |
1.4347 |
293.15 |
0.0000 |
1.333 |
293.15 |
0.1000 |
1.3894 |
293.15 |
0.2000 |
1.4083 |
293.15 |
0.2999 |
1.4174 |
293.15 |
0.4000 |
1.4224 |
293.15 |
0.5000 |
1.4253 |
293.15 |
0.6000 |
1.4273 |
293.15 |
0.7000 |
1.4289 |
293.15 |
0.7998 |
1.4299 |
293.15 |
0.8999 |
1.4307 |
293.15 |
1.0000 |
1.4312 |
303.15 |
0.0000 |
1.3319 |
303.15 |
0.1000 |
1.387 |
303.15 |
0.2000 |
1.4057 |
303.15 |
0.2999 |
1.4146 |
303.15 |
0.4000 |
1.4194 |
303.15 |
0.5000 |
1.4224 |
303.15 |
0.6000 |
1.4243 |
303.15 |
0.7000 |
1.4258 |
303.15 |
0.7998 |
1.4267 |
303.15 |
0.8999 |
1.4275 |
303.15 |
1.0000 |
1.4281 |
313.15 |
0.0000 |
1.3306 |
313.15 |
0.1000 |
1.3842 |
313.15 |
0.2000 |
1.4022 |
313.15 |
0.2999 |
1.4109 |
313.15 |
0.4000 |
1.4157 |
313.15 |
0.5000 |
1.4185 |
313.15 |
0.6000 |
1.4204 |
313.15 |
0.7000 |
1.4219 |
313.15 |
0.7998 |
1.4227 |
313.15 |
0.8999 |
1.4234 |
313.15 |
1.0000 |
1.424 |
323.15 |
0.0000 |
1.329 |
323.15 |
0.1000 |
1.3808 |
323.15 |
0.2000 |
1.3982 |
323.15 |
0.2999 |
1.4067 |
323.15 |
0.4000 |
1.4113 |
323.15 |
0.5000 |
1.4141 |
323.15 |
0.6000 |
1.4159 |
323.15 |
0.7000 |
1.4172 |
323.15 |
0.7998 |
1.4182 |
323.15 |
0.8999 |
1.4188 |
323.15 |
1.0000 |
1.4194 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0000 |
1.3325 |
0.0010 |
1.3339 |
0.0020 |
1.3356 |
0.0050 |
1.338 |
0.0075 |
1.3415 |
0.0098 |
1.3426 |
0.0125 |
1.346 |
0.0250 |
1.3551 |
0.0252 |
1.3563 |
0.0502 |
1.3703 |
0.0753 |
1.38 |
0.1012 |
1.3886 |
0.1511 |
1.3995 |
0.2014 |
1.4072 |
0.3030 |
1.4152 |
0.4021 |
1.4203 |
0.4939 |
1.4229 |
0.6049 |
1.4251 |
0.7064 |
1.4269 |
0.7988 |
1.4276 |
0.8948 |
1.4284 |
1.0000 |
1.4295 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Refractive index (Na D-line) - Liquid |
283.15 |
0.0000 |
1.3337 |
283.15 |
0.1000 |
1.3916 |
283.15 |
0.2000 |
1.411 |
283.15 |
0.2999 |
1.4204 |
283.15 |
0.4000 |
1.4255 |
283.15 |
0.5000 |
1.4286 |
283.15 |
0.6000 |
1.4307 |
283.15 |
0.7000 |
1.4323 |
283.15 |
0.7998 |
1.4334 |
283.15 |
0.8999 |
1.4342 |
283.15 |
1.0000 |
1.4347 |
293.15 |
0.0000 |
1.333 |
293.15 |
0.1000 |
1.3894 |
293.15 |
0.2000 |
1.4083 |
293.15 |
0.2999 |
1.4174 |
293.15 |
0.4000 |
1.4224 |
293.15 |
0.5000 |
1.4253 |
293.15 |
0.6000 |
1.4273 |
293.15 |
0.7000 |
1.4289 |
293.15 |
0.7998 |
1.4299 |
293.15 |
0.8999 |
1.4307 |
293.15 |
1.0000 |
1.4312 |
303.15 |
0.0000 |
1.3319 |
303.15 |
0.1000 |
1.387 |
303.15 |
0.2000 |
1.4057 |
303.15 |
0.2999 |
1.4146 |
303.15 |
0.4000 |
1.4194 |
303.15 |
0.5000 |
1.4224 |
303.15 |
0.6000 |
1.4243 |
303.15 |
0.7000 |
1.4258 |
303.15 |
0.7998 |
1.4267 |
303.15 |
0.8999 |
1.4275 |
303.15 |
1.0000 |
1.4281 |
313.15 |
0.0000 |
1.3306 |
313.15 |
0.1000 |
1.3842 |
313.15 |
0.2000 |
1.4022 |
313.15 |
0.2999 |
1.4109 |
313.15 |
0.4000 |
1.4157 |
313.15 |
0.5000 |
1.4185 |
313.15 |
0.6000 |
1.4204 |
313.15 |
0.7000 |
1.4219 |
313.15 |
0.7998 |
1.4227 |
313.15 |
0.8999 |
1.4234 |
313.15 |
1.0000 |
1.424 |
323.15 |
0.0000 |
1.329 |
323.15 |
0.1000 |
1.3808 |
323.15 |
0.2000 |
1.3982 |
323.15 |
0.2999 |
1.4067 |
323.15 |
0.4000 |
1.4113 |
323.15 |
0.5000 |
1.4141 |
323.15 |
0.6000 |
1.4159 |
323.15 |
0.7000 |
1.4172 |
323.15 |
0.7998 |
1.4182 |
323.15 |
0.8999 |
1.4188 |
323.15 |
1.0000 |
1.4194 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0000 |
1.3325 |
0.0010 |
1.3339 |
0.0020 |
1.3356 |
0.0050 |
1.338 |
0.0075 |
1.3415 |
0.0098 |
1.3426 |
0.0125 |
1.346 |
0.0250 |
1.3551 |
0.0252 |
1.3563 |
0.0502 |
1.3703 |
0.0753 |
1.38 |
0.1012 |
1.3886 |
0.1511 |
1.3995 |
0.2014 |
1.4072 |
0.3030 |
1.4152 |
0.4021 |
1.4203 |
0.4939 |
1.4229 |
0.6049 |
1.4251 |
0.7064 |
1.4269 |
0.7988 |
1.4276 |
0.8948 |
1.4284 |
1.0000 |
1.4295 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Mass density, kg/m3 - Liquid |
303.15 |
101.30 |
0.0800 |
996.7 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0000 |
998.2 |
293.15 |
0.0122 |
1000.9 |
293.15 |
0.0271 |
1001.9 |
293.15 |
0.0454 |
1000.6 |
293.15 |
0.0689 |
997.8 |
293.15 |
0.0998 |
994.1 |
293.15 |
0.1428 |
990.1 |
293.15 |
0.2062 |
984.3 |
293.15 |
0.3078 |
976.8 |
293.15 |
0.4037 |
971.1 |
293.15 |
0.5015 |
966.4 |
293.15 |
0.6107 |
962.4 |
293.15 |
0.7050 |
959.5 |
293.15 |
0.7958 |
957.1 |
293.15 |
0.8932 |
954.9 |
293.15 |
1.0000 |
952.9 |
303.15 |
0.0000 |
995.7 |
303.15 |
0.0122 |
996.8 |
303.15 |
0.0271 |
996.4 |
303.15 |
0.0454 |
993.4 |
303.15 |
0.0689 |
990.7 |
303.15 |
0.0998 |
986.6 |
303.15 |
0.1428 |
981.8 |
303.15 |
0.2062 |
975.7 |
303.15 |
0.3078 |
967.9 |
303.15 |
0.4037 |
961.8 |
303.15 |
0.5015 |
957.1 |
303.15 |
0.6107 |
953.0 |
303.15 |
0.7050 |
950.1 |
303.15 |
0.7958 |
947.7 |
303.15 |
0.8932 |
945.5 |
303.15 |
1.0000 |
943.5 |
313.15 |
0.0000 |
992.2 |
313.15 |
0.0122 |
992.3 |
313.15 |
0.0271 |
990.6 |
313.15 |
0.0454 |
987.4 |
313.15 |
0.0689 |
983.9 |
313.15 |
0.0998 |
979.3 |
313.15 |
0.1428 |
974.2 |
313.15 |
0.2062 |
967.7 |
313.15 |
0.3078 |
959.9 |
313.15 |
0.4037 |
953.9 |
313.15 |
0.5015 |
949.2 |
313.15 |
0.6107 |
945.1 |
313.15 |
0.7050 |
942.2 |
313.15 |
0.7958 |
939.8 |
313.15 |
0.8932 |
937.7 |
313.15 |
1.0000 |
935.7 |
323.15 |
0.0000 |
988.1 |
323.15 |
0.0122 |
987.0 |
323.15 |
0.0271 |
984.9 |
323.15 |
0.0454 |
980.6 |
323.15 |
0.0689 |
976.2 |
323.15 |
0.0998 |
971.6 |
323.15 |
0.1428 |
965.8 |
323.15 |
0.2062 |
958.9 |
323.15 |
0.3078 |
950.8 |
323.15 |
0.4037 |
944.8 |
323.15 |
0.5015 |
940.1 |
323.15 |
0.6107 |
936.0 |
323.15 |
0.7050 |
933.1 |
323.15 |
0.7958 |
930.7 |
323.15 |
0.8932 |
928.6 |
323.15 |
1.0000 |
926.6 |
333.15 |
0.0000 |
983.2 |
333.15 |
0.0122 |
981.4 |
333.15 |
0.0271 |
978.8 |
333.15 |
0.0454 |
974.1 |
333.15 |
0.0689 |
969.0 |
333.15 |
0.0998 |
964.3 |
333.15 |
0.1428 |
958.0 |
333.15 |
0.2062 |
950.8 |
333.15 |
0.3078 |
942.6 |
333.15 |
0.4037 |
936.7 |
333.15 |
0.5015 |
931.9 |
333.15 |
0.6107 |
927.9 |
333.15 |
0.7050 |
924.9 |
333.15 |
0.7958 |
922.6 |
333.15 |
0.8932 |
920.4 |
333.15 |
1.0000 |
918.5 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.0000 |
999.7 |
283.15 |
0.0020 |
1000.2 |
283.15 |
0.0030 |
1000.41 |
283.15 |
0.0050 |
1001.05 |
283.15 |
0.0062 |
1001.43 |
283.15 |
0.0071 |
1001.75 |
283.15 |
0.0079 |
1002.0 |
283.15 |
0.0089 |
1002.32 |
283.15 |
0.0099 |
1002.65 |
283.15 |
0.0149 |
1004.27 |
283.15 |
0.0206 |
1005.74 |
283.15 |
0.0238 |
1006.36 |
283.15 |
0.0270 |
1006.66 |
283.15 |
0.0301 |
1006.78 |
283.15 |
0.0395 |
1006.53 |
283.15 |
0.0604 |
1005.13 |
283.15 |
0.0799 |
1003.42 |
283.15 |
0.1000 |
1001.67 |
283.15 |
0.2000 |
992.63 |
283.15 |
0.2999 |
985.44 |
283.15 |
0.4000 |
979.51 |
283.15 |
0.5000 |
974.9 |
283.15 |
0.6000 |
971.46 |
283.15 |
0.7000 |
968.77 |
283.15 |
0.7998 |
966.62 |
283.15 |
0.8999 |
964.58 |
283.15 |
1.0000 |
962.57 |
283.15 |
0.0000 |
999.7 |
293.15 |
0.0000 |
998.2 |
293.15 |
0.0020 |
998.59 |
293.15 |
0.0030 |
998.79 |
293.15 |
0.0050 |
999.2 |
293.15 |
0.0062 |
999.48 |
293.15 |
0.0071 |
999.68 |
293.15 |
0.0079 |
999.88 |
293.15 |
0.0089 |
1000.11 |
293.15 |
0.0099 |
1000.34 |
293.15 |
0.0149 |
1001.44 |
293.15 |
0.0206 |
1002.03 |
293.15 |
0.0238 |
1002.2 |
293.15 |
0.0270 |
1002.11 |
293.15 |
0.0301 |
1001.94 |
293.15 |
0.0395 |
1001.04 |
293.15 |
0.0604 |
998.81 |
293.15 |
0.0799 |
996.64 |
293.15 |
0.1000 |
994.55 |
293.15 |
0.2000 |
984.71 |
293.15 |
0.2999 |
977.27 |
293.15 |
0.4000 |
971.27 |
293.15 |
0.5000 |
966.63 |
293.15 |
0.6000 |
963.17 |
293.15 |
0.7000 |
960.45 |
293.15 |
0.7998 |
958.25 |
293.15 |
0.8999 |
956.18 |
293.15 |
1.0000 |
954.16 |
293.15 |
0.0000 |
998.2 |
303.15 |
0.0000 |
995.65 |
303.15 |
0.0020 |
995.87 |
303.15 |
0.0030 |
996.01 |
303.15 |
0.0050 |
996.31 |
303.15 |
0.0062 |
996.53 |
303.15 |
0.0071 |
996.67 |
303.15 |
0.0079 |
996.81 |
303.15 |
0.0089 |
996.95 |
303.15 |
0.0099 |
997.07 |
303.15 |
0.0149 |
997.66 |
303.15 |
0.0206 |
997.51 |
303.15 |
0.0238 |
997.18 |
303.15 |
0.0270 |
997.0 |
303.15 |
0.0301 |
996.61 |
303.15 |
0.0395 |
995.23 |
303.15 |
0.0604 |
992.28 |
303.15 |
0.0799 |
989.68 |
303.15 |
0.1000 |
987.21 |
303.15 |
0.2000 |
976.63 |
303.15 |
0.2999 |
968.97 |
303.15 |
0.4000 |
962.91 |
303.15 |
0.5000 |
958.27 |
303.15 |
0.6000 |
954.74 |
303.15 |
0.7000 |
952.05 |
303.15 |
0.7998 |
949.8 |
303.15 |
0.8999 |
947.72 |
303.15 |
1.0000 |
945.74 |
303.15 |
0.0000 |
995.65 |
313.15 |
0.0000 |
992.21 |
313.15 |
0.0020 |
992.68 |
313.15 |
0.0030 |
992.86 |
313.15 |
0.0050 |
993.28 |
313.15 |
0.0062 |
993.43 |
313.15 |
0.0071 |
993.51 |
313.15 |
0.0079 |
993.62 |
313.15 |
0.0089 |
993.66 |
313.15 |
0.0099 |
993.71 |
313.15 |
0.0149 |
993.62 |
313.15 |
0.0206 |
993.05 |
313.15 |
0.0238 |
992.61 |
313.15 |
0.0270 |
992.19 |
313.15 |
0.0301 |
991.64 |
313.15 |
0.0395 |
989.79 |
313.15 |
0.0604 |
986.16 |
313.15 |
0.0799 |
983.24 |
313.15 |
0.1000 |
979.73 |
313.15 |
0.2000 |
968.47 |
313.15 |
0.2999 |
960.58 |
313.15 |
0.4000 |
954.51 |
313.15 |
0.5000 |
949.82 |
313.15 |
0.6000 |
946.32 |
313.15 |
0.7000 |
943.62 |
313.15 |
0.7998 |
941.34 |
313.15 |
0.8999 |
939.34 |
313.15 |
1.0000 |
937.35 |
313.15 |
0.0000 |
992.21 |
323.15 |
0.0000 |
988.04 |
323.15 |
0.1000 |
971.95 |
323.15 |
0.2000 |
960.1 |
323.15 |
0.2999 |
951.9 |
323.15 |
0.4000 |
945.89 |
323.15 |
0.5000 |
941.29 |
323.15 |
0.6000 |
937.75 |
323.15 |
0.7000 |
935.03 |
323.15 |
0.7998 |
932.8 |
323.15 |
0.8999 |
930.8 |
323.15 |
1.0000 |
928.85 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
997.05 |
0.0010 |
997.04 |
0.0020 |
997.13 |
0.0050 |
997.6 |
0.0075 |
998.1 |
0.0098 |
998.56 |
0.0125 |
999.03 |
0.0250 |
999.25 |
0.0252 |
999.25 |
0.0502 |
996.46 |
0.0753 |
993.48 |
0.1012 |
990.25 |
0.1511 |
985.47 |
0.2014 |
980.54 |
0.3030 |
973.56 |
0.4021 |
967.48 |
0.4939 |
964.01 |
0.6049 |
959.05 |
0.7064 |
956.27 |
0.7988 |
954.15 |
0.8948 |
952.06 |
1.0000 |
950.41 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Mass density, kg/m3 - Liquid |
303.15 |
101.30 |
0.0800 |
996.7 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0000 |
998.2 |
293.15 |
0.0122 |
1000.9 |
293.15 |
0.0271 |
1001.9 |
293.15 |
0.0454 |
1000.6 |
293.15 |
0.0689 |
997.8 |
293.15 |
0.0998 |
994.1 |
293.15 |
0.1428 |
990.1 |
293.15 |
0.2062 |
984.3 |
293.15 |
0.3078 |
976.8 |
293.15 |
0.4037 |
971.1 |
293.15 |
0.5015 |
966.4 |
293.15 |
0.6107 |
962.4 |
293.15 |
0.7050 |
959.5 |
293.15 |
0.7958 |
957.1 |
293.15 |
0.8932 |
954.9 |
293.15 |
1.0000 |
952.9 |
303.15 |
0.0000 |
995.7 |
303.15 |
0.0122 |
996.8 |
303.15 |
0.0271 |
996.4 |
303.15 |
0.0454 |
993.4 |
303.15 |
0.0689 |
990.7 |
303.15 |
0.0998 |
986.6 |
303.15 |
0.1428 |
981.8 |
303.15 |
0.2062 |
975.7 |
303.15 |
0.3078 |
967.9 |
303.15 |
0.4037 |
961.8 |
303.15 |
0.5015 |
957.1 |
303.15 |
0.6107 |
953.0 |
303.15 |
0.7050 |
950.1 |
303.15 |
0.7958 |
947.7 |
303.15 |
0.8932 |
945.5 |
303.15 |
1.0000 |
943.5 |
313.15 |
0.0000 |
992.2 |
313.15 |
0.0122 |
992.3 |
313.15 |
0.0271 |
990.6 |
313.15 |
0.0454 |
987.4 |
313.15 |
0.0689 |
983.9 |
313.15 |
0.0998 |
979.3 |
313.15 |
0.1428 |
974.2 |
313.15 |
0.2062 |
967.7 |
313.15 |
0.3078 |
959.9 |
313.15 |
0.4037 |
953.9 |
313.15 |
0.5015 |
949.2 |
313.15 |
0.6107 |
945.1 |
313.15 |
0.7050 |
942.2 |
313.15 |
0.7958 |
939.8 |
313.15 |
0.8932 |
937.7 |
313.15 |
1.0000 |
935.7 |
323.15 |
0.0000 |
988.1 |
323.15 |
0.0122 |
987.0 |
323.15 |
0.0271 |
984.9 |
323.15 |
0.0454 |
980.6 |
323.15 |
0.0689 |
976.2 |
323.15 |
0.0998 |
971.6 |
323.15 |
0.1428 |
965.8 |
323.15 |
0.2062 |
958.9 |
323.15 |
0.3078 |
950.8 |
323.15 |
0.4037 |
944.8 |
323.15 |
0.5015 |
940.1 |
323.15 |
0.6107 |
936.0 |
323.15 |
0.7050 |
933.1 |
323.15 |
0.7958 |
930.7 |
323.15 |
0.8932 |
928.6 |
323.15 |
1.0000 |
926.6 |
333.15 |
0.0000 |
983.2 |
333.15 |
0.0122 |
981.4 |
333.15 |
0.0271 |
978.8 |
333.15 |
0.0454 |
974.1 |
333.15 |
0.0689 |
969.0 |
333.15 |
0.0998 |
964.3 |
333.15 |
0.1428 |
958.0 |
333.15 |
0.2062 |
950.8 |
333.15 |
0.3078 |
942.6 |
333.15 |
0.4037 |
936.7 |
333.15 |
0.5015 |
931.9 |
333.15 |
0.6107 |
927.9 |
333.15 |
0.7050 |
924.9 |
333.15 |
0.7958 |
922.6 |
333.15 |
0.8932 |
920.4 |
333.15 |
1.0000 |
918.5 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.0000 |
999.7 |
283.15 |
0.0020 |
1000.2 |
283.15 |
0.0030 |
1000.41 |
283.15 |
0.0050 |
1001.05 |
283.15 |
0.0062 |
1001.43 |
283.15 |
0.0071 |
1001.75 |
283.15 |
0.0079 |
1002.0 |
283.15 |
0.0089 |
1002.32 |
283.15 |
0.0099 |
1002.65 |
283.15 |
0.0149 |
1004.27 |
283.15 |
0.0206 |
1005.74 |
283.15 |
0.0238 |
1006.36 |
283.15 |
0.0270 |
1006.66 |
283.15 |
0.0301 |
1006.78 |
283.15 |
0.0395 |
1006.53 |
283.15 |
0.0604 |
1005.13 |
283.15 |
0.0799 |
1003.42 |
283.15 |
0.1000 |
1001.67 |
283.15 |
0.2000 |
992.63 |
283.15 |
0.2999 |
985.44 |
283.15 |
0.4000 |
979.51 |
283.15 |
0.5000 |
974.9 |
283.15 |
0.6000 |
971.46 |
283.15 |
0.7000 |
968.77 |
283.15 |
0.7998 |
966.62 |
283.15 |
0.8999 |
964.58 |
283.15 |
1.0000 |
962.57 |
283.15 |
0.0000 |
999.7 |
293.15 |
0.0000 |
998.2 |
293.15 |
0.0020 |
998.59 |
293.15 |
0.0030 |
998.79 |
293.15 |
0.0050 |
999.2 |
293.15 |
0.0062 |
999.48 |
293.15 |
0.0071 |
999.68 |
293.15 |
0.0079 |
999.88 |
293.15 |
0.0089 |
1000.11 |
293.15 |
0.0099 |
1000.34 |
293.15 |
0.0149 |
1001.44 |
293.15 |
0.0206 |
1002.03 |
293.15 |
0.0238 |
1002.2 |
293.15 |
0.0270 |
1002.11 |
293.15 |
0.0301 |
1001.94 |
293.15 |
0.0395 |
1001.04 |
293.15 |
0.0604 |
998.81 |
293.15 |
0.0799 |
996.64 |
293.15 |
0.1000 |
994.55 |
293.15 |
0.2000 |
984.71 |
293.15 |
0.2999 |
977.27 |
293.15 |
0.4000 |
971.27 |
293.15 |
0.5000 |
966.63 |
293.15 |
0.6000 |
963.17 |
293.15 |
0.7000 |
960.45 |
293.15 |
0.7998 |
958.25 |
293.15 |
0.8999 |
956.18 |
293.15 |
1.0000 |
954.16 |
293.15 |
0.0000 |
998.2 |
303.15 |
0.0000 |
995.65 |
303.15 |
0.0020 |
995.87 |
303.15 |
0.0030 |
996.01 |
303.15 |
0.0050 |
996.31 |
303.15 |
0.0062 |
996.53 |
303.15 |
0.0071 |
996.67 |
303.15 |
0.0079 |
996.81 |
303.15 |
0.0089 |
996.95 |
303.15 |
0.0099 |
997.07 |
303.15 |
0.0149 |
997.66 |
303.15 |
0.0206 |
997.51 |
303.15 |
0.0238 |
997.18 |
303.15 |
0.0270 |
997.0 |
303.15 |
0.0301 |
996.61 |
303.15 |
0.0395 |
995.23 |
303.15 |
0.0604 |
992.28 |
303.15 |
0.0799 |
989.68 |
303.15 |
0.1000 |
987.21 |
303.15 |
0.2000 |
976.63 |
303.15 |
0.2999 |
968.97 |
303.15 |
0.4000 |
962.91 |
303.15 |
0.5000 |
958.27 |
303.15 |
0.6000 |
954.74 |
303.15 |
0.7000 |
952.05 |
303.15 |
0.7998 |
949.8 |
303.15 |
0.8999 |
947.72 |
303.15 |
1.0000 |
945.74 |
303.15 |
0.0000 |
995.65 |
313.15 |
0.0000 |
992.21 |
313.15 |
0.0020 |
992.68 |
313.15 |
0.0030 |
992.86 |
313.15 |
0.0050 |
993.28 |
313.15 |
0.0062 |
993.43 |
313.15 |
0.0071 |
993.51 |
313.15 |
0.0079 |
993.62 |
313.15 |
0.0089 |
993.66 |
313.15 |
0.0099 |
993.71 |
313.15 |
0.0149 |
993.62 |
313.15 |
0.0206 |
993.05 |
313.15 |
0.0238 |
992.61 |
313.15 |
0.0270 |
992.19 |
313.15 |
0.0301 |
991.64 |
313.15 |
0.0395 |
989.79 |
313.15 |
0.0604 |
986.16 |
313.15 |
0.0799 |
983.24 |
313.15 |
0.1000 |
979.73 |
313.15 |
0.2000 |
968.47 |
313.15 |
0.2999 |
960.58 |
313.15 |
0.4000 |
954.51 |
313.15 |
0.5000 |
949.82 |
313.15 |
0.6000 |
946.32 |
313.15 |
0.7000 |
943.62 |
313.15 |
0.7998 |
941.34 |
313.15 |
0.8999 |
939.34 |
313.15 |
1.0000 |
937.35 |
313.15 |
0.0000 |
992.21 |
323.15 |
0.0000 |
988.04 |
323.15 |
0.1000 |
971.95 |
323.15 |
0.2000 |
960.1 |
323.15 |
0.2999 |
951.9 |
323.15 |
0.4000 |
945.89 |
323.15 |
0.5000 |
941.29 |
323.15 |
0.6000 |
937.75 |
323.15 |
0.7000 |
935.03 |
323.15 |
0.7998 |
932.8 |
323.15 |
0.8999 |
930.8 |
323.15 |
1.0000 |
928.85 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
997.05 |
0.0010 |
997.04 |
0.0020 |
997.13 |
0.0050 |
997.6 |
0.0075 |
998.1 |
0.0098 |
998.56 |
0.0125 |
999.03 |
0.0250 |
999.25 |
0.0252 |
999.25 |
0.0502 |
996.46 |
0.0753 |
993.48 |
0.1012 |
990.25 |
0.1511 |
985.47 |
0.2014 |
980.54 |
0.3030 |
973.56 |
0.4021 |
967.48 |
0.4939 |
964.01 |
0.6049 |
959.05 |
0.7064 |
956.27 |
0.7988 |
954.15 |
0.8948 |
952.06 |
1.0000 |
950.41 |
Speed of sound, m/s
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Speed of sound, m/s - Liquid |
0.0000 |
1496.7 |
0.0010 |
1507.7 |
0.0020 |
1513.9 |
0.0050 |
1526.2 |
0.0075 |
1544.6 |
0.0098 |
1555.2 |
0.0125 |
1564.8 |
0.0250 |
1571.7 |
0.0252 |
1566.2 |
0.0502 |
1546.2 |
0.0753 |
1532.8 |
0.1012 |
1515.2 |
0.1511 |
1494.4 |
0.2014 |
1481.7 |
0.3030 |
1453.3 |
0.4021 |
1422.4 |
0.4939 |
1409.6 |
0.6049 |
1395.2 |
0.7064 |
1384.0 |
0.7988 |
1379.2 |
0.8948 |
1369.6 |
1.0000 |
1360.0 |
Speed of sound, m/s
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid |
Speed of sound, m/s - Liquid |
0.0000 |
1496.7 |
0.0010 |
1507.7 |
0.0020 |
1513.9 |
0.0050 |
1526.2 |
0.0075 |
1544.6 |
0.0098 |
1555.2 |
0.0125 |
1564.8 |
0.0250 |
1571.7 |
0.0252 |
1566.2 |
0.0502 |
1546.2 |
0.0753 |
1532.8 |
0.1012 |
1515.2 |
0.1511 |
1494.4 |
0.2014 |
1481.7 |
0.3030 |
1453.3 |
0.4021 |
1422.4 |
0.4939 |
1409.6 |
0.6049 |
1395.2 |
0.7064 |
1384.0 |
0.7988 |
1379.2 |
0.8948 |
1369.6 |
1.0000 |
1360.0 |
Sources