Mixture of Ethane, 1,2-dibromo- + Heptane

Datasets

1. C_p,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
2. ρ_l - Mass density, kg/m3 (2)
3. c_sound,fluid - Speed of Sound, m/s (2)

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
293.15	0.1016	213.58
293.15	0.2016	204.39
293.15	0.2989	196.15
293.15	0.3977	187.73
293.15	0.4996	179.31
293.15	0.5991	170.59
293.15	0.6928	162.47
293.15	0.8022	153.18
293.15	0.9003	144.90
293.15	1.0000	136.87
294.15	0.1016	213.90
294.15	0.2016	204.73
294.15	0.2989	196.48
294.15	0.3977	188.03
294.15	0.4996	179.43
294.15	0.5991	170.80
294.15	0.6928	162.60
294.15	0.8022	153.26
294.15	0.9003	144.94
294.15	1.0000	136.90
295.15	0.1016	214.26
295.15	0.2016	204.92
295.15	0.2989	196.66
295.15	0.3977	188.20
295.15	0.4996	179.65
295.15	0.5991	170.96
295.15	0.6928	162.81
295.15	0.8022	153.40
295.15	0.9003	145.07
295.15	1.0000	136.95
296.15	0.1016	214.59
296.15	0.2016	205.30
296.15	0.2989	196.95
296.15	0.3977	188.51
296.15	0.4996	179.89
296.15	0.5991	171.13
296.15	0.6928	162.90
296.15	0.8022	153.53
296.15	0.9003	145.16
296.15	1.0000	136.99
297.15	0.1016	214.90
297.15	0.2016	205.51
297.15	0.2989	197.29
297.15	0.3977	188.66
297.15	0.4996	180.09
297.15	0.5991	171.23
297.15	0.6928	163.05
297.15	0.8022	153.63
297.15	0.9003	145.24
297.15	1.0000	137.02
298.15	0.1016	215.25
298.15	0.2016	205.83
298.15	0.2989	197.53
298.15	0.3977	188.94
298.15	0.4996	180.26
298.15	0.5991	171.40
298.15	0.6928	163.18
298.15	0.8022	153.72
298.15	0.9003	145.27
298.15	1.0000	137.04
299.15	0.1016	215.55
299.15	0.2016	206.18
299.15	0.2989	197.72
299.15	0.3977	189.11
299.15	0.4996	180.39
299.15	0.5991	171.55
299.15	0.6928	163.24
299.15	0.8022	153.84
299.15	0.9003	145.33
299.15	1.0000	137.09
300.15	0.1016	215.90
300.15	0.2016	206.45
300.15	0.2989	198.00
300.15	0.3977	189.43
300.15	0.4996	180.66
300.15	0.5991	171.77
300.15	0.6928	163.47
300.15	0.8022	153.91
300.15	0.9003	145.40
300.15	1.0000	137.11
301.15	0.1016	216.32
301.15	0.2016	206.71
301.15	0.2989	198.31
301.15	0.3977	189.64
301.15	0.4996	180.79
301.15	0.5991	171.90
301.15	0.6928	163.50
301.15	0.8022	153.98
301.15	0.9003	145.47
301.15	1.0000	137.15
302.15	0.1016	216.60
302.15	0.2016	207.03
302.15	0.2989	198.60
302.15	0.3977	189.82
302.15	0.4996	181.03
302.15	0.5991	172.01
302.15	0.6928	163.71
302.15	0.8022	154.13
302.15	0.9003	145.60
302.15	1.0000	137.20
303.15	0.1016	216.95
303.15	0.2016	207.33
303.15	0.2989	198.77
303.15	0.3977	190.01
303.15	0.4996	181.17
303.15	0.5991	172.23
303.15	0.6928	163.89
303.15	0.8022	154.24
303.15	0.9003	145.65
303.15	1.0000	137.25
304.15	0.1016	217.33
304.15	0.2016	207.57
304.15	0.2989	199.17
304.15	0.3977	190.33
304.15	0.4996	181.40
304.15	0.5991	172.31
304.15	0.6928	163.94
304.15	0.8022	154.32
304.15	0.9003	145.75
304.15	1.0000	137.29
305.15	0.1016	217.70
305.15	0.2016	207.95
305.15	0.2989	199.39
305.15	0.3977	190.62
305.15	0.4996	181.54
305.15	0.5991	172.49
305.15	0.6928	164.06
305.15	0.8022	154.37
305.15	0.9003	145.77
305.15	1.0000	137.32
306.15	0.1016	218.07
306.15	0.2016	208.28
306.15	0.2989	199.58
306.15	0.3977	190.75
306.15	0.4996	181.72
306.15	0.5991	172.71
306.15	0.6928	164.29
306.15	0.8022	154.55
306.15	0.9003	145.83
306.15	1.0000	137.39
307.15	0.1016	218.39
307.15	0.2016	208.47
307.15	0.2989	199.90
307.15	0.3977	191.03
307.15	0.4996	181.95
307.15	0.5991	172.88
307.15	0.6928	164.40
307.15	0.8022	154.60
307.15	0.9003	145.96
307.15	1.0000	137.42
308.15	0.1016	218.69
308.15	0.2016	208.80
308.15	0.2989	200.20
308.15	0.3977	191.31
308.15	0.4996	182.17
308.15	0.5991	173.00
308.15	0.6928	164.48
308.15	0.8022	154.68
308.15	0.9003	146.01
308.15	1.0000	137.49
309.15	0.1016	219.10
309.15	0.2016	209.10
309.15	0.2989	200.37
309.15	0.3977	191.50
309.15	0.4996	182.37
309.15	0.5991	173.19
309.15	0.6928	164.70
309.15	0.8022	154.79
309.15	0.9003	146.13
309.15	1.0000	137.53
310.15	0.1016	219.41
310.15	0.2016	209.50
310.15	0.2989	200.65
310.15	0.3977	191.66
310.15	0.4996	182.48
310.15	0.5991	173.29
310.15	0.6928	164.80
310.15	0.8022	154.90
310.15	0.9003	146.20
310.15	1.0000	137.60
311.15	0.1016	219.69
311.15	0.2016	209.78
311.15	0.2989	200.99
311.15	0.3977	191.91
311.15	0.4996	182.68
311.15	0.5991	173.50
311.15	0.6928	164.88
311.15	0.8022	155.00
311.15	0.9003	146.21
311.15	1.0000	137.65
312.15	0.1016	220.11
312.15	0.2016	210.10
312.15	0.2989	201.15
312.15	0.3977	192.12
312.15	0.4996	182.91
312.15	0.5991	173.69
312.15	0.6928	165.06
312.15	0.8022	155.16
312.15	0.9003	146.30
312.15	1.0000	137.71
313.15	0.1016	220.35
313.15	0.2016	210.39
313.15	0.2989	201.51
313.15	0.3977	192.42
313.15	0.4996	183.06
313.15	0.5991	173.84
313.15	0.6928	165.16
313.15	0.8022	155.25
313.15	0.9003	146.43
313.15	1.0000	137.77

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
293.15	0.1016	213.58
293.15	0.2016	204.39
293.15	0.2989	196.15
293.15	0.3977	187.73
293.15	0.4996	179.31
293.15	0.5991	170.59
293.15	0.6928	162.47
293.15	0.8022	153.18
293.15	0.9003	144.90
293.15	1.0000	136.87
294.15	0.1016	213.90
294.15	0.2016	204.73
294.15	0.2989	196.48
294.15	0.3977	188.03
294.15	0.4996	179.43
294.15	0.5991	170.80
294.15	0.6928	162.60
294.15	0.8022	153.26
294.15	0.9003	144.94
294.15	1.0000	136.90
295.15	0.1016	214.26
295.15	0.2016	204.92
295.15	0.2989	196.66
295.15	0.3977	188.20
295.15	0.4996	179.65
295.15	0.5991	170.96
295.15	0.6928	162.81
295.15	0.8022	153.40
295.15	0.9003	145.07
295.15	1.0000	136.95
296.15	0.1016	214.59
296.15	0.2016	205.30
296.15	0.2989	196.95
296.15	0.3977	188.51
296.15	0.4996	179.89
296.15	0.5991	171.13
296.15	0.6928	162.90
296.15	0.8022	153.53
296.15	0.9003	145.16
296.15	1.0000	136.99
297.15	0.1016	214.90
297.15	0.2016	205.51
297.15	0.2989	197.29
297.15	0.3977	188.66
297.15	0.4996	180.09
297.15	0.5991	171.23
297.15	0.6928	163.05
297.15	0.8022	153.63
297.15	0.9003	145.24
297.15	1.0000	137.02
298.15	0.1016	215.25
298.15	0.2016	205.83
298.15	0.2989	197.53
298.15	0.3977	188.94
298.15	0.4996	180.26
298.15	0.5991	171.40
298.15	0.6928	163.18
298.15	0.8022	153.72
298.15	0.9003	145.27
298.15	1.0000	137.04
299.15	0.1016	215.55
299.15	0.2016	206.18
299.15	0.2989	197.72
299.15	0.3977	189.11
299.15	0.4996	180.39
299.15	0.5991	171.55
299.15	0.6928	163.24
299.15	0.8022	153.84
299.15	0.9003	145.33
299.15	1.0000	137.09
300.15	0.1016	215.90
300.15	0.2016	206.45
300.15	0.2989	198.00
300.15	0.3977	189.43
300.15	0.4996	180.66
300.15	0.5991	171.77
300.15	0.6928	163.47
300.15	0.8022	153.91
300.15	0.9003	145.40
300.15	1.0000	137.11
301.15	0.1016	216.32
301.15	0.2016	206.71
301.15	0.2989	198.31
301.15	0.3977	189.64
301.15	0.4996	180.79
301.15	0.5991	171.90
301.15	0.6928	163.50
301.15	0.8022	153.98
301.15	0.9003	145.47
301.15	1.0000	137.15
302.15	0.1016	216.60
302.15	0.2016	207.03
302.15	0.2989	198.60
302.15	0.3977	189.82
302.15	0.4996	181.03
302.15	0.5991	172.01
302.15	0.6928	163.71
302.15	0.8022	154.13
302.15	0.9003	145.60
302.15	1.0000	137.20
303.15	0.1016	216.95
303.15	0.2016	207.33
303.15	0.2989	198.77
303.15	0.3977	190.01
303.15	0.4996	181.17
303.15	0.5991	172.23
303.15	0.6928	163.89
303.15	0.8022	154.24
303.15	0.9003	145.65
303.15	1.0000	137.25
304.15	0.1016	217.33
304.15	0.2016	207.57
304.15	0.2989	199.17
304.15	0.3977	190.33
304.15	0.4996	181.40
304.15	0.5991	172.31
304.15	0.6928	163.94
304.15	0.8022	154.32
304.15	0.9003	145.75
304.15	1.0000	137.29
305.15	0.1016	217.70
305.15	0.2016	207.95
305.15	0.2989	199.39
305.15	0.3977	190.62
305.15	0.4996	181.54
305.15	0.5991	172.49
305.15	0.6928	164.06
305.15	0.8022	154.37
305.15	0.9003	145.77
305.15	1.0000	137.32
306.15	0.1016	218.07
306.15	0.2016	208.28
306.15	0.2989	199.58
306.15	0.3977	190.75
306.15	0.4996	181.72
306.15	0.5991	172.71
306.15	0.6928	164.29
306.15	0.8022	154.55
306.15	0.9003	145.83
306.15	1.0000	137.39
307.15	0.1016	218.39
307.15	0.2016	208.47
307.15	0.2989	199.90
307.15	0.3977	191.03
307.15	0.4996	181.95
307.15	0.5991	172.88
307.15	0.6928	164.40
307.15	0.8022	154.60
307.15	0.9003	145.96
307.15	1.0000	137.42
308.15	0.1016	218.69
308.15	0.2016	208.80
308.15	0.2989	200.20
308.15	0.3977	191.31
308.15	0.4996	182.17
308.15	0.5991	173.00
308.15	0.6928	164.48
308.15	0.8022	154.68
308.15	0.9003	146.01
308.15	1.0000	137.49
309.15	0.1016	219.10
309.15	0.2016	209.10
309.15	0.2989	200.37
309.15	0.3977	191.50
309.15	0.4996	182.37
309.15	0.5991	173.19
309.15	0.6928	164.70
309.15	0.8022	154.79
309.15	0.9003	146.13
309.15	1.0000	137.53
310.15	0.1016	219.41
310.15	0.2016	209.50
310.15	0.2989	200.65
310.15	0.3977	191.66
310.15	0.4996	182.48
310.15	0.5991	173.29
310.15	0.6928	164.80
310.15	0.8022	154.90
310.15	0.9003	146.20
310.15	1.0000	137.60
311.15	0.1016	219.69
311.15	0.2016	209.78
311.15	0.2989	200.99
311.15	0.3977	191.91
311.15	0.4996	182.68
311.15	0.5991	173.50
311.15	0.6928	164.88
311.15	0.8022	155.00
311.15	0.9003	146.21
311.15	1.0000	137.65
312.15	0.1016	220.11
312.15	0.2016	210.10
312.15	0.2989	201.15
312.15	0.3977	192.12
312.15	0.4996	182.91
312.15	0.5991	173.69
312.15	0.6928	165.06
312.15	0.8022	155.16
312.15	0.9003	146.30
312.15	1.0000	137.71
313.15	0.1016	220.35
313.15	0.2016	210.39
313.15	0.2989	201.51
313.15	0.3977	192.42
313.15	0.4996	183.06
313.15	0.5991	173.84
313.15	0.6928	165.16
313.15	0.8022	155.25
313.15	0.9003	146.43
313.15	1.0000	137.77

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	683.82
293.15	0.1018	776.01
293.15	0.2052	878.46
293.15	0.2931	973.9
293.15	0.3754	1070.54
293.15	0.3919	1091.09
293.15	0.5009	1234.71
293.15	0.5993	1379.31
293.15	0.6916	1530.51
293.15	0.7886	1707.97
293.15	0.8919	1922.0
293.15	1.0000	2178.77
298.15	0.0000	679.59
298.15	0.1018	771.16
298.15	0.2052	872.98
298.15	0.2931	968.0
298.15	0.3754	1064.3
298.15	0.3919	1084.74
298.15	0.5009	1227.73
298.15	0.5993	1372.04
298.15	0.6916	1522.49
298.15	0.7886	1699.34
298.15	0.8919	1912.55
298.15	1.0000	2168.41
303.15	0.0000	675.31
303.15	0.1018	766.4
303.15	0.2052	867.72
303.15	0.2931	962.23
303.15	0.3754	1058.0
303.15	0.3919	1078.36
303.15	0.5009	1220.93
303.15	0.5993	1364.69
303.15	0.6916	1514.35
303.15	0.7886	1690.56
303.15	0.8919	1903.13
303.15	1.0000	2157.94
308.15	0.0000	671.02
308.15	0.1018	761.38
308.15	0.2052	862.14
308.15	0.2931	956.31
308.15	0.3754	1051.8
308.15	0.3919	1071.93
308.15	0.5009	1213.97
308.15	0.5993	1357.19
308.15	0.6916	1506.3
308.15	0.7886	1681.76
308.15	0.8919	1893.55
308.15	1.0000	2147.47
313.15	0.0000	666.68
313.15	0.1018	756.39
313.15	0.2052	856.68
313.15	0.2931	950.37
313.15	0.3754	1045.35
313.15	0.3919	1065.57
313.15	0.5009	1207.14
313.15	0.5993	1349.51
313.15	0.6916	1498.2
313.15	0.7886	1673.14
313.15	0.8919	1884.12
313.15	1.0000	2136.96

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	683.82
293.15	0.1018	776.01
293.15	0.2052	878.46
293.15	0.2931	973.9
293.15	0.3754	1070.54
293.15	0.3919	1091.09
293.15	0.5009	1234.71
293.15	0.5993	1379.31
293.15	0.6916	1530.51
293.15	0.7886	1707.97
293.15	0.8919	1922.0
293.15	1.0000	2178.77
298.15	0.0000	679.59
298.15	0.1018	771.16
298.15	0.2052	872.98
298.15	0.2931	968.0
298.15	0.3754	1064.3
298.15	0.3919	1084.74
298.15	0.5009	1227.73
298.15	0.5993	1372.04
298.15	0.6916	1522.49
298.15	0.7886	1699.34
298.15	0.8919	1912.55
298.15	1.0000	2168.41
303.15	0.0000	675.31
303.15	0.1018	766.4
303.15	0.2052	867.72
303.15	0.2931	962.23
303.15	0.3754	1058.0
303.15	0.3919	1078.36
303.15	0.5009	1220.93
303.15	0.5993	1364.69
303.15	0.6916	1514.35
303.15	0.7886	1690.56
303.15	0.8919	1903.13
303.15	1.0000	2157.94
308.15	0.0000	671.02
308.15	0.1018	761.38
308.15	0.2052	862.14
308.15	0.2931	956.31
308.15	0.3754	1051.8
308.15	0.3919	1071.93
308.15	0.5009	1213.97
308.15	0.5993	1357.19
308.15	0.6916	1506.3
308.15	0.7886	1681.76
308.15	0.8919	1893.55
308.15	1.0000	2147.47
313.15	0.0000	666.68
313.15	0.1018	756.39
313.15	0.2052	856.68
313.15	0.2931	950.37
313.15	0.3754	1045.35
313.15	0.3919	1065.57
313.15	0.5009	1207.14
313.15	0.5993	1349.51
313.15	0.6916	1498.2
313.15	0.7886	1673.14
313.15	0.8919	1884.12
313.15	1.0000	2136.96

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid	Speed of sound, m/s - Liquid
292.60	0.6005	996.77
292.62	0.2000	1079.5
292.64	0.1024	1112.12
292.64	0.2986	1050.76
292.66	0.6997	989.87
292.68	0.4002	1027.19
292.68	0.8004	989.25
292.70	0.4996	1009.41
292.70	0.9061	995.84
292.84	1.0000	1007.52
298.56	0.1024	1087.95
298.56	0.9061	980.0
298.58	0.2000	1056.48
298.59	0.4996	990.17
298.59	0.6005	978.03
298.60	0.4002	1006.69
298.60	0.6997	972.29
298.68	0.8004	972.17
298.69	0.2986	1028.57
299.17	1.0000	991.14
303.37	1.0000	980.18
303.54	0.4002	989.74
303.57	0.9061	966.53
303.59	0.1024	1067.66
303.61	0.2000	1037.19
303.61	0.6997	957.6
303.62	0.6005	962.51
303.65	0.2986	1010.63
303.66	0.4996	973.72
303.78	0.8004	957.87
308.44	0.9061	953.47
308.57	0.6997	943.03
308.58	0.4002	972.63
308.59	0.6005	947.22
308.59	0.8004	944.46
308.62	0.1024	1047.39
308.62	0.2986	992.63
308.65	0.2000	1017.99
308.75	1.0000	966.56
309.57	0.4996	954.55
314.45	1.0000	952.0
314.52	0.9061	937.35
314.55	0.6997	925.53
314.56	0.2000	995.72
314.58	0.4002	952.25
314.58	0.8004	927.74
314.59	0.1024	1023.62
314.59	0.4996	938.54
314.59	0.6005	928.96
314.61	0.2986	971.18

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid	Speed of sound, m/s - Liquid
292.60	0.6005	996.77
292.62	0.2000	1079.5
292.64	0.1024	1112.12
292.64	0.2986	1050.76
292.66	0.6997	989.87
292.68	0.4002	1027.19
292.68	0.8004	989.25
292.70	0.4996	1009.41
292.70	0.9061	995.84
292.84	1.0000	1007.52
298.56	0.1024	1087.95
298.56	0.9061	980.0
298.58	0.2000	1056.48
298.59	0.4996	990.17
298.59	0.6005	978.03
298.60	0.4002	1006.69
298.60	0.6997	972.29
298.68	0.8004	972.17
298.69	0.2986	1028.57
299.17	1.0000	991.14
303.37	1.0000	980.18
303.54	0.4002	989.74
303.57	0.9061	966.53
303.59	0.1024	1067.66
303.61	0.2000	1037.19
303.61	0.6997	957.6
303.62	0.6005	962.51
303.65	0.2986	1010.63
303.66	0.4996	973.72
303.78	0.8004	957.87
308.44	0.9061	953.47
308.57	0.6997	943.03
308.58	0.4002	972.63
308.59	0.6005	947.22
308.59	0.8004	944.46
308.62	0.1024	1047.39
308.62	0.2986	992.63
308.65	0.2000	1017.99
308.75	1.0000	966.56
309.57	0.4996	954.55
314.45	1.0000	952.0
314.52	0.9061	937.35
314.55	0.6997	925.53
314.56	0.2000	995.72
314.58	0.4002	952.25
314.58	0.8004	927.74
314.59	0.1024	1023.62
314.59	0.4996	938.54
314.59	0.6005	928.96
314.61	0.2986	971.18

Sources

• Thermophysical and Acoustical Properties of the Binary Mixtures 1,2-Dibromoethane + Heptane within the Temperature Range from 293.15 K to 313.15 K