Mixture of Diethyl carbonate + Cyclohexane, methyl-

Datasets

1. Mole fraction (2)
2. η - Viscosity, Pa*s (2)
3. ρ_l - Mass density, kg/m3 (2)
4. c_sound,fluid - Speed of Sound, m/s (2)
5. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Cyclohexane, methyl- (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Cyclohexane, methyl- (2) - Liquid	Mole fraction of Cyclohexane, methyl- (2) - Gas
0.0079	0.0223
0.0296	0.1002
0.0696	0.2058
0.0963	0.2651
0.1263	0.3325
0.1796	0.4123
0.2246	0.4702
0.2532	0.5036
0.2973	0.5496
0.3227	0.5736
0.3614	0.6123
0.3958	0.6352
0.4659	0.6712
0.4925	0.6932
0.5162	0.7063
0.5523	0.7256
0.6123	0.7569
0.6478	0.7736
0.6785	0.7953
0.7122	0.8025
0.7479	0.8186
0.7839	0.8365
0.8226	0.8563
0.8635	0.8879
0.9057	0.9159
0.9523	0.9535

Mole fraction of Cyclohexane, methyl- (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Cyclohexane, methyl- (2) - Liquid	Mole fraction of Cyclohexane, methyl- (2) - Gas
0.0079	0.0223
0.0296	0.1002
0.0696	0.2058
0.0963	0.2651
0.1263	0.3325
0.1796	0.4123
0.2246	0.4702
0.2532	0.5036
0.2973	0.5496
0.3227	0.5736
0.3614	0.6123
0.3958	0.6352
0.4659	0.6712
0.4925	0.6932
0.5162	0.7063
0.5523	0.7256
0.6123	0.7569
0.6478	0.7736
0.6785	0.7953
0.7122	0.8025
0.7479	0.8186
0.7839	0.8365
0.8226	0.8563
0.8635	0.8879
0.9057	0.9159
0.9523	0.9535

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0007
293.15	0.0473	0.0007
293.15	0.0978	0.0007
293.15	0.1985	0.0007
293.15	0.2968	0.0007
293.15	0.3924	0.0007
293.15	0.4993	0.0007
293.15	0.5999	0.0007
293.15	0.6985	0.0007
293.15	0.7988	0.0007
293.15	0.8996	0.0008
293.15	0.9509	0.0008
293.15	1.0000	0.0008
298.15	0.0000	0.0007
298.15	0.0473	0.0007
298.15	0.0978	0.0006
298.15	0.1985	0.0006
298.15	0.2968	0.0006
298.15	0.3924	0.0006
298.15	0.4993	0.0006
298.15	0.5999	0.0006
298.15	0.6985	0.0007
298.15	0.7988	0.0007
298.15	0.8996	0.0007
298.15	0.9509	0.0007
298.15	1.0000	0.0008
303.15	0.0000	0.0006
303.15	0.0473	0.0006
303.15	0.0978	0.0006
303.15	0.1985	0.0006
303.15	0.2968	0.0006
303.15	0.3924	0.0006
303.15	0.4993	0.0006
303.15	0.5999	0.0006
303.15	0.6985	0.0006
303.15	0.7988	0.0006
303.15	0.8996	0.0007
303.15	0.9509	0.0007
303.15	1.0000	0.0007
308.15	0.0000	0.0006
308.15	0.0473	0.0006
308.15	0.0978	0.0006
308.15	0.1985	0.0006
308.15	0.2968	0.0006
308.15	0.3924	0.0006
308.15	0.4993	0.0006
308.15	0.5999	0.0006
308.15	0.6985	0.0006
308.15	0.7988	0.0006
308.15	0.8996	0.0006
308.15	0.9509	0.0006
308.15	1.0000	0.0007
313.15	0.0000	0.0006
313.15	0.0473	0.0005
313.15	0.0978	0.0005
313.15	0.1985	0.0005
313.15	0.2968	0.0005
313.15	0.3924	0.0005
313.15	0.4993	0.0005
313.15	0.5999	0.0005
313.15	0.6985	0.0006
313.15	0.7988	0.0006
313.15	0.8996	0.0006
313.15	0.9509	0.0006
313.15	1.0000	0.0006

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0007
293.15	0.0473	0.0007
293.15	0.0978	0.0007
293.15	0.1985	0.0007
293.15	0.2968	0.0007
293.15	0.3924	0.0007
293.15	0.4993	0.0007
293.15	0.5999	0.0007
293.15	0.6985	0.0007
293.15	0.7988	0.0007
293.15	0.8996	0.0008
293.15	0.9509	0.0008
293.15	1.0000	0.0008
298.15	0.0000	0.0007
298.15	0.0473	0.0007
298.15	0.0978	0.0006
298.15	0.1985	0.0006
298.15	0.2968	0.0006
298.15	0.3924	0.0006
298.15	0.4993	0.0006
298.15	0.5999	0.0006
298.15	0.6985	0.0007
298.15	0.7988	0.0007
298.15	0.8996	0.0007
298.15	0.9509	0.0007
298.15	1.0000	0.0008
303.15	0.0000	0.0006
303.15	0.0473	0.0006
303.15	0.0978	0.0006
303.15	0.1985	0.0006
303.15	0.2968	0.0006
303.15	0.3924	0.0006
303.15	0.4993	0.0006
303.15	0.5999	0.0006
303.15	0.6985	0.0006
303.15	0.7988	0.0006
303.15	0.8996	0.0007
303.15	0.9509	0.0007
303.15	1.0000	0.0007
308.15	0.0000	0.0006
308.15	0.0473	0.0006
308.15	0.0978	0.0006
308.15	0.1985	0.0006
308.15	0.2968	0.0006
308.15	0.3924	0.0006
308.15	0.4993	0.0006
308.15	0.5999	0.0006
308.15	0.6985	0.0006
308.15	0.7988	0.0006
308.15	0.8996	0.0006
308.15	0.9509	0.0006
308.15	1.0000	0.0007
313.15	0.0000	0.0006
313.15	0.0473	0.0005
313.15	0.0978	0.0005
313.15	0.1985	0.0005
313.15	0.2968	0.0005
313.15	0.3924	0.0005
313.15	0.4993	0.0005
313.15	0.5999	0.0005
313.15	0.6985	0.0006
313.15	0.7988	0.0006
313.15	0.8996	0.0006
313.15	0.9509	0.0006
313.15	1.0000	0.0006

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	769.3
293.15	0.0473	777.44
293.15	0.0978	786.43
293.15	0.1985	804.96
293.15	0.2968	823.73
293.15	0.3924	842.56
293.15	0.4993	864.26
293.15	0.5999	885.33
293.15	0.6985	906.48
293.15	0.7988	928.64
293.15	0.8996	951.53
293.15	0.9509	963.41
293.15	1.0000	974.83
298.15	0.0000	764.98
298.15	0.0473	773.05
298.15	0.0978	781.97
298.15	0.1985	800.36
298.15	0.2968	818.99
298.15	0.3924	837.7
298.15	0.4993	859.23
298.15	0.5999	880.2
298.15	0.6985	901.24
298.15	0.7988	923.28
298.15	0.8996	946.06
298.15	0.9509	957.86
298.15	1.0000	969.24
303.15	0.0000	760.65
303.15	0.0473	768.64
303.15	0.0978	777.5
303.15	0.1985	795.73
303.15	0.2968	814.23
303.15	0.3924	832.8
303.15	0.4993	854.18
303.15	0.5999	875.04
303.15	0.6985	895.95
303.15	0.7988	917.88
303.15	0.8996	940.54
303.15	0.9509	952.29
303.15	1.0000	963.61
308.15	0.0000	756.29
308.15	0.0473	764.22
308.15	0.0978	773.0
308.15	0.1985	791.09
308.15	0.2968	809.44
308.15	0.3924	827.88
308.15	0.4993	849.14
308.15	0.5999	869.85
308.15	0.6985	890.65
308.15	0.7988	912.46
308.15	0.8996	935.01
308.15	0.9509	946.7
308.15	1.0000	957.96
313.15	0.0000	751.93
313.15	0.0473	759.78
313.15	0.0978	768.48
313.15	0.1985	786.42
313.15	0.2968	804.6
313.15	0.3924	822.9
313.15	0.4993	844.04
313.15	0.5999	864.64
313.15	0.6985	885.31
313.15	0.7988	907.02
313.15	0.8996	929.44
313.15	0.9509	941.08
313.15	1.0000	952.29

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	769.3
293.15	0.0473	777.44
293.15	0.0978	786.43
293.15	0.1985	804.96
293.15	0.2968	823.73
293.15	0.3924	842.56
293.15	0.4993	864.26
293.15	0.5999	885.33
293.15	0.6985	906.48
293.15	0.7988	928.64
293.15	0.8996	951.53
293.15	0.9509	963.41
293.15	1.0000	974.83
298.15	0.0000	764.98
298.15	0.0473	773.05
298.15	0.0978	781.97
298.15	0.1985	800.36
298.15	0.2968	818.99
298.15	0.3924	837.7
298.15	0.4993	859.23
298.15	0.5999	880.2
298.15	0.6985	901.24
298.15	0.7988	923.28
298.15	0.8996	946.06
298.15	0.9509	957.86
298.15	1.0000	969.24
303.15	0.0000	760.65
303.15	0.0473	768.64
303.15	0.0978	777.5
303.15	0.1985	795.73
303.15	0.2968	814.23
303.15	0.3924	832.8
303.15	0.4993	854.18
303.15	0.5999	875.04
303.15	0.6985	895.95
303.15	0.7988	917.88
303.15	0.8996	940.54
303.15	0.9509	952.29
303.15	1.0000	963.61
308.15	0.0000	756.29
308.15	0.0473	764.22
308.15	0.0978	773.0
308.15	0.1985	791.09
308.15	0.2968	809.44
308.15	0.3924	827.88
308.15	0.4993	849.14
308.15	0.5999	869.85
308.15	0.6985	890.65
308.15	0.7988	912.46
308.15	0.8996	935.01
308.15	0.9509	946.7
308.15	1.0000	957.96
313.15	0.0000	751.93
313.15	0.0473	759.78
313.15	0.0978	768.48
313.15	0.1985	786.42
313.15	0.2968	804.6
313.15	0.3924	822.9
313.15	0.4993	844.04
313.15	0.5999	864.64
313.15	0.6985	885.31
313.15	0.7988	907.02
313.15	0.8996	929.44
313.15	0.9509	941.08
313.15	1.0000	952.29

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1237.0
293.15	0.0473	1229.0
293.15	0.0978	1222.0
293.15	0.1985	1211.0
293.15	0.2968	1203.0
293.15	0.3924	1196.0
293.15	0.4993	1192.0
293.15	0.5999	1189.0
293.15	0.6985	1189.0
293.15	0.7988	1191.0
293.15	0.8996	1194.0
293.15	0.9509	1196.0
293.15	1.0000	1198.0
298.15	0.0000	1215.0
298.15	0.0473	1207.0
298.15	0.0978	1201.0
298.15	0.1985	1189.0
298.15	0.2968	1181.0
298.15	0.3924	1175.0
298.15	0.4993	1171.0
298.15	0.5999	1168.0
298.15	0.6985	1168.0
298.15	0.7988	1170.0
298.15	0.8996	1173.0
298.15	0.9509	1175.0
298.15	1.0000	1177.0
303.15	0.0000	1193.0
303.15	0.0473	1185.0
303.15	0.0978	1179.0
303.15	0.1985	1168.0
303.15	0.2968	1160.0
303.15	0.3924	1154.0
303.15	0.4993	1149.0
303.15	0.5999	1147.0
303.15	0.6985	1147.0
303.15	0.7988	1149.0
303.15	0.8996	1152.0
303.15	0.9509	1155.0
303.15	1.0000	1157.0
308.15	0.0000	1172.0
308.15	0.0473	1164.0
308.15	0.0978	1157.0
308.15	0.1985	1146.0
308.15	0.2968	1138.0
308.15	0.3924	1132.0
308.15	0.4993	1128.0
308.15	0.5999	1126.0
308.15	0.6985	1126.0
308.15	0.7988	1128.0
308.15	0.8996	1132.0
308.15	0.9509	1134.0
308.15	1.0000	1136.0
313.15	0.0000	1150.0
313.15	0.0473	1142.0
313.15	0.0978	1136.0
313.15	0.1985	1125.0
313.15	0.2968	1117.0
313.15	0.3924	1111.0
313.15	0.4993	1107.0
313.15	0.5999	1105.0
313.15	0.6985	1106.0
313.15	0.7988	1108.0
313.15	0.8996	1112.0
313.15	0.9509	1114.0
313.15	1.0000	1116.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1237.0
293.15	0.0473	1229.0
293.15	0.0978	1222.0
293.15	0.1985	1211.0
293.15	0.2968	1203.0
293.15	0.3924	1196.0
293.15	0.4993	1192.0
293.15	0.5999	1189.0
293.15	0.6985	1189.0
293.15	0.7988	1191.0
293.15	0.8996	1194.0
293.15	0.9509	1196.0
293.15	1.0000	1198.0
298.15	0.0000	1215.0
298.15	0.0473	1207.0
298.15	0.0978	1201.0
298.15	0.1985	1189.0
298.15	0.2968	1181.0
298.15	0.3924	1175.0
298.15	0.4993	1171.0
298.15	0.5999	1168.0
298.15	0.6985	1168.0
298.15	0.7988	1170.0
298.15	0.8996	1173.0
298.15	0.9509	1175.0
298.15	1.0000	1177.0
303.15	0.0000	1193.0
303.15	0.0473	1185.0
303.15	0.0978	1179.0
303.15	0.1985	1168.0
303.15	0.2968	1160.0
303.15	0.3924	1154.0
303.15	0.4993	1149.0
303.15	0.5999	1147.0
303.15	0.6985	1147.0
303.15	0.7988	1149.0
303.15	0.8996	1152.0
303.15	0.9509	1155.0
303.15	1.0000	1157.0
308.15	0.0000	1172.0
308.15	0.0473	1164.0
308.15	0.0978	1157.0
308.15	0.1985	1146.0
308.15	0.2968	1138.0
308.15	0.3924	1132.0
308.15	0.4993	1128.0
308.15	0.5999	1126.0
308.15	0.6985	1126.0
308.15	0.7988	1128.0
308.15	0.8996	1132.0
308.15	0.9509	1134.0
308.15	1.0000	1136.0
313.15	0.0000	1150.0
313.15	0.0473	1142.0
313.15	0.0978	1136.0
313.15	0.1985	1125.0
313.15	0.2968	1117.0
313.15	0.3924	1111.0
313.15	0.4993	1107.0
313.15	0.5999	1105.0
313.15	0.6985	1106.0
313.15	0.7988	1108.0
313.15	0.8996	1112.0
313.15	0.9509	1114.0
313.15	1.0000	1116.0

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Cyclohexane, methyl- (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0079	398.09
0.0296	396.87
0.0696	392.92
0.0963	391.10
0.1263	389.74
0.1796	387.31
0.2246	385.47
0.2532	383.50
0.2973	382.24
0.3227	381.19
0.3614	380.18
0.3958	379.44
0.4659	378.10
0.4925	377.92
0.5162	377.92
0.5523	377.13
0.6123	376.22
0.6478	376.04
0.6785	375.60
0.7122	375.38
0.7479	375.02
0.7839	374.66
0.8226	374.50
0.8635	374.21
0.9057	374.05
0.9523	373.98

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Cyclohexane, methyl- (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0079	398.09
0.0296	396.87
0.0696	392.92
0.0963	391.10
0.1263	389.74
0.1796	387.31
0.2246	385.47
0.2532	383.50
0.2973	382.24
0.3227	381.19
0.3614	380.18
0.3958	379.44
0.4659	378.10
0.4925	377.92
0.5162	377.92
0.5523	377.13
0.6123	376.22
0.6478	376.04
0.6785	375.60
0.7122	375.38
0.7479	375.02
0.7839	374.66
0.8226	374.50
0.8635	374.21
0.9057	374.05
0.9523	373.98

Sources

• VLE of the binary systems (dimethyl carbonate with 2-propanol or 2-butanol) and (diethyl carbonate with methylcyclohexane) at 101.3 kPa
• Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures