Mixture of n-Propyl chloride + Tetrahydrofuran

Datasets

1. Mole fraction (8)
2. P_vap - Vapor or sublimation pressure, kPa (2)
3. n₀ - Refractive index (Na D-line) (2)
4. ρ_l - Mass density, kg/m3 (2)
5. c_sound,fluid - Speed of Sound, m/s (2)
6. T_boil - Boiling temperature at pressure P, K (6)

Mole fraction of Tetrahydrofuran (2) [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Mole fraction of Tetrahydrofuran (2) - Gas
0.0437	0.0153
0.0966	0.0405
0.2056	0.0997
0.3047	0.1672
0.4022	0.2425
0.5075	0.3346
0.6174	0.4566
0.7161	0.5772
0.8111	0.6999
0.9003	0.8415
0.9485	0.9200

Mole fraction of Tetrahydrofuran (2) [ref]

Operational condition: Pressure, kPa = 70 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Mole fraction of Tetrahydrofuran (2) - Gas
0.0431	0.0185
0.1232	0.0563
0.1949	0.0971
0.2993	0.1687
0.3945	0.2415
0.5001	0.3448
0.6101	0.4608
0.7125	0.5781
0.7947	0.6958
0.8986	0.8437
0.9515	0.9298

Mole fraction of Tetrahydrofuran (2) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Mole fraction of Tetrahydrofuran (2) - Gas
0.0468	0.0158
0.0914	0.0384
0.2112	0.1117
0.3062	0.1831
0.3974	0.2576
0.5071	0.3589
0.6097	0.4777
0.7183	0.6046
0.8027	0.7129
0.9033	0.8547
0.9451	0.9166

Mole fraction of Tetrahydrofuran (2) [ref]

Fixed		Measured
Mole fraction of Tetrahydrofuran (2) - Liquid	Temperature, K - Liquid	Mole fraction of Tetrahydrofuran (2) - Gas
0.0592	298.15	0.0287
0.0592	313.15	0.0255
0.0985	298.15	0.0405
0.0985	313.15	0.0415
0.1910	298.15	0.0992
0.1920	313.15	0.1126
0.3170	313.15	0.1898
0.3280	298.15	0.1739
0.4103	298.15	0.2384
0.4103	313.15	0.2502
0.5160	298.15	0.3363
0.5280	313.15	0.3805
0.5903	298.15	0.4181
0.5906	313.15	0.4253
0.6850	298.15	0.5230
0.6860	313.15	0.5308
0.7620	298.15	0.6199
0.7620	313.15	0.6233
0.8180	298.15	0.6913
0.8180	313.15	0.7005
0.8740	298.15	0.7912
0.8770	313.15	0.7915
0.9230	298.15	0.8525
0.9330	313.15	0.8805
0.9560	298.15	0.9109
0.9560	313.15	0.9280

Mole fraction of Tetrahydrofuran (2) [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Mole fraction of Tetrahydrofuran (2) - Gas
0.0437	0.0153
0.0966	0.0405
0.2056	0.0997
0.3047	0.1672
0.4022	0.2425
0.5075	0.3346
0.6174	0.4566
0.7161	0.5772
0.8111	0.6999
0.9003	0.8415
0.9485	0.9200

Mole fraction of Tetrahydrofuran (2) [ref]

Operational condition: Pressure, kPa = 70 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Mole fraction of Tetrahydrofuran (2) - Gas
0.0431	0.0185
0.1232	0.0563
0.1949	0.0971
0.2993	0.1687
0.3945	0.2415
0.5001	0.3448
0.6101	0.4608
0.7125	0.5781
0.7947	0.6958
0.8986	0.8437
0.9515	0.9298

Mole fraction of Tetrahydrofuran (2) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Mole fraction of Tetrahydrofuran (2) - Gas
0.0468	0.0158
0.0914	0.0384
0.2112	0.1117
0.3062	0.1831
0.3974	0.2576
0.5071	0.3589
0.6097	0.4777
0.7183	0.6046
0.8027	0.7129
0.9033	0.8547
0.9451	0.9166

Mole fraction of Tetrahydrofuran (2) [ref]

Fixed		Measured
Mole fraction of Tetrahydrofuran (2) - Liquid	Temperature, K - Liquid	Mole fraction of Tetrahydrofuran (2) - Gas
0.0592	298.15	0.0287
0.0592	313.15	0.0255
0.0985	298.15	0.0405
0.0985	313.15	0.0415
0.1910	298.15	0.0992
0.1920	313.15	0.1126
0.3170	313.15	0.1898
0.3280	298.15	0.1739
0.4103	298.15	0.2384
0.4103	313.15	0.2502
0.5160	298.15	0.3363
0.5280	313.15	0.3805
0.5903	298.15	0.4181
0.5906	313.15	0.4253
0.6850	298.15	0.5230
0.6860	313.15	0.5308
0.7620	298.15	0.6199
0.7620	313.15	0.6233
0.8180	298.15	0.6913
0.8180	313.15	0.7005
0.8740	298.15	0.7912
0.8770	313.15	0.7915
0.9230	298.15	0.8525
0.9330	313.15	0.8805
0.9560	298.15	0.9109
0.9560	313.15	0.9280

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Tetrahydrofuran (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0592	298.15	44.20
0.0592	313.15	77.94
0.0985	298.15	43.12
0.0985	313.15	76.28
0.1910	298.15	40.76
0.1920	313.15	72.00
0.3170	313.15	66.67
0.3280	298.15	37.01
0.4103	298.15	35.02
0.4103	313.15	62.56
0.5160	298.15	32.38
0.5280	313.15	57.73
0.5903	298.15	30.59
0.5906	313.15	55.34
0.6850	298.15	28.30
0.6860	313.15	51.66
0.7620	298.15	26.66
0.7620	313.15	48.80
0.8180	298.15	25.25
0.8180	313.15	46.91
0.8740	298.15	24.11
0.8770	313.15	44.66
0.9230	298.15	23.23
0.9330	313.15	42.74
0.9560	298.15	22.41
0.9560	313.15	42.01

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Tetrahydrofuran (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0592	298.15	44.20
0.0592	313.15	77.94
0.0985	298.15	43.12
0.0985	313.15	76.28
0.1910	298.15	40.76
0.1920	313.15	72.00
0.3170	313.15	66.67
0.3280	298.15	37.01
0.4103	298.15	35.02
0.4103	313.15	62.56
0.5160	298.15	32.38
0.5280	313.15	57.73
0.5903	298.15	30.59
0.5906	313.15	55.34
0.6850	298.15	28.30
0.6860	313.15	51.66
0.7620	298.15	26.66
0.7620	313.15	48.80
0.8180	298.15	25.25
0.8180	313.15	46.91
0.8740	298.15	24.11
0.8770	313.15	44.66
0.9230	298.15	23.23
0.9330	313.15	42.74
0.9560	298.15	22.41
0.9560	313.15	42.01

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydrofuran (2) - Liquid	Refractive index (Na D-line) - Liquid
283.15	0.0000	1.3943
283.15	0.0446	1.3952
283.15	0.0884	1.3962
283.15	0.2139	1.3987
283.15	0.2695	1.3998
283.15	0.3754	1.4019
283.15	0.4714	1.4037
283.15	0.5751	1.4055
283.15	0.6721	1.4072
283.15	0.7779	1.409
283.15	0.8857	1.4108
283.15	0.9441	1.4117
283.15	1.0000	1.4126
298.15	0.0000	1.3855
298.15	0.0452	1.3865
298.15	0.0879	1.3874
298.15	0.1893	1.3896
298.15	0.2882	1.3917
298.15	0.3851	1.3937
298.15	0.4863	1.3957
298.15	0.5834	1.3975
298.15	0.6865	1.3994
298.15	0.7917	1.4012
298.15	0.8997	1.403
298.15	0.9426	1.4037
298.15	1.0000	1.4046
313.15	0.0000	1.3764
313.15	0.0426	1.3775
313.15	0.0862	1.3785
313.15	0.1800	1.3807
313.15	0.2772	1.3828
313.15	0.3731	1.3849
313.15	0.4772	1.387
313.15	0.5736	1.3889
313.15	0.6836	1.391
313.15	0.7805	1.3928
313.15	0.9075	1.395
313.15	0.9449	1.3956
313.15	1.0000	1.3966

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydrofuran (2) - Liquid	Refractive index (Na D-line) - Liquid
283.15	0.0000	1.3943
283.15	0.0446	1.3952
283.15	0.0884	1.3962
283.15	0.2139	1.3987
283.15	0.2695	1.3998
283.15	0.3754	1.4019
283.15	0.4714	1.4037
283.15	0.5751	1.4055
283.15	0.6721	1.4072
283.15	0.7779	1.409
283.15	0.8857	1.4108
283.15	0.9441	1.4117
283.15	1.0000	1.4126
298.15	0.0000	1.3855
298.15	0.0452	1.3865
298.15	0.0879	1.3874
298.15	0.1893	1.3896
298.15	0.2882	1.3917
298.15	0.3851	1.3937
298.15	0.4863	1.3957
298.15	0.5834	1.3975
298.15	0.6865	1.3994
298.15	0.7917	1.4012
298.15	0.8997	1.403
298.15	0.9426	1.4037
298.15	1.0000	1.4046
313.15	0.0000	1.3764
313.15	0.0426	1.3775
313.15	0.0862	1.3785
313.15	0.1800	1.3807
313.15	0.2772	1.3828
313.15	0.3731	1.3849
313.15	0.4772	1.387
313.15	0.5736	1.3889
313.15	0.6836	1.391
313.15	0.7805	1.3928
313.15	0.9075	1.395
313.15	0.9449	1.3956
313.15	1.0000	1.3966

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydrofuran (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	902.42
283.15	0.0482	902.34
283.15	0.0951	902.3
283.15	0.2278	902.3
283.15	0.2856	902.25
283.15	0.3945	902.02
283.15	0.4915	901.73
283.15	0.5947	901.21
283.15	0.6896	900.63
283.15	0.7915	899.88
283.15	0.8936	899.0
283.15	0.9482	898.5
283.15	1.0000	898.0
298.15	0.0000	883.29
298.15	0.0490	883.46
298.15	0.0949	883.63
298.15	0.2025	884.0
298.15	0.3057	884.24
298.15	0.4052	884.36
298.15	0.5073	884.31
298.15	0.6037	884.14
298.15	0.7043	883.79
298.15	0.8052	883.3
298.15	0.9070	882.71
298.15	0.9470	882.44
298.15	1.0000	882.05
313.15	0.0000	864.69
313.15	0.0463	864.94
313.15	0.0932	865.25
313.15	0.1931	865.84
313.15	0.2948	866.3
313.15	0.3935	866.63
313.15	0.4987	866.79
313.15	0.5945	866.81
313.15	0.7020	866.65
313.15	0.7949	866.39
313.15	0.9145	865.88
313.15	0.9492	865.69
313.15	1.0000	865.36

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydrofuran (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	902.42
283.15	0.0482	902.34
283.15	0.0951	902.3
283.15	0.2278	902.3
283.15	0.2856	902.25
283.15	0.3945	902.02
283.15	0.4915	901.73
283.15	0.5947	901.21
283.15	0.6896	900.63
283.15	0.7915	899.88
283.15	0.8936	899.0
283.15	0.9482	898.5
283.15	1.0000	898.0
298.15	0.0000	883.29
298.15	0.0490	883.46
298.15	0.0949	883.63
298.15	0.2025	884.0
298.15	0.3057	884.24
298.15	0.4052	884.36
298.15	0.5073	884.31
298.15	0.6037	884.14
298.15	0.7043	883.79
298.15	0.8052	883.3
298.15	0.9070	882.71
298.15	0.9470	882.44
298.15	1.0000	882.05
313.15	0.0000	864.69
313.15	0.0463	864.94
313.15	0.0932	865.25
313.15	0.1931	865.84
313.15	0.2948	866.3
313.15	0.3935	866.63
313.15	0.4987	866.79
313.15	0.5945	866.81
313.15	0.7020	866.65
313.15	0.7949	866.39
313.15	0.9145	865.88
313.15	0.9492	865.69
313.15	1.0000	865.36

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydrofuran (2) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0000	1130.6
283.15	0.0482	1140.5
283.15	0.0951	1149.3
283.15	0.2278	1175.5
283.15	0.2856	1187.1
283.15	0.3945	1209.5
283.15	0.4915	1230.5
283.15	0.5947	1253.3
283.15	0.6896	1275.5
283.15	0.7915	1299.5
283.15	0.8936	1324.2
283.15	0.9482	1337.4
283.15	1.0000	1350.9
298.15	0.0000	1065.5
298.15	0.0490	1075.0
298.15	0.0949	1083.6
298.15	0.2025	1104.4
298.15	0.3057	1124.8
298.15	0.4052	1145.3
298.15	0.5073	1167.1
298.15	0.6037	1188.2
298.15	0.7043	1210.5
298.15	0.8052	1233.0
298.15	0.9070	1256.7
298.15	0.9470	1265.8
298.15	1.0000	1278.8
313.15	0.0000	1000.5
313.15	0.0463	1009.8
313.15	0.0932	1018.8
313.15	0.1931	1037.4
313.15	0.2948	1057.0
313.15	0.3935	1076.8
313.15	0.4987	1098.0
313.15	0.5945	1117.9
313.15	0.7020	1140.6
313.15	0.7949	1160.4
313.15	0.9145	1186.7
313.15	0.9492	1194.9
313.15	1.0000	1206.4

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydrofuran (2) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0000	1130.6
283.15	0.0482	1140.5
283.15	0.0951	1149.3
283.15	0.2278	1175.5
283.15	0.2856	1187.1
283.15	0.3945	1209.5
283.15	0.4915	1230.5
283.15	0.5947	1253.3
283.15	0.6896	1275.5
283.15	0.7915	1299.5
283.15	0.8936	1324.2
283.15	0.9482	1337.4
283.15	1.0000	1350.9
298.15	0.0000	1065.5
298.15	0.0490	1075.0
298.15	0.0949	1083.6
298.15	0.2025	1104.4
298.15	0.3057	1124.8
298.15	0.4052	1145.3
298.15	0.5073	1167.1
298.15	0.6037	1188.2
298.15	0.7043	1210.5
298.15	0.8052	1233.0
298.15	0.9070	1256.7
298.15	0.9470	1265.8
298.15	1.0000	1278.8
313.15	0.0000	1000.5
313.15	0.0463	1009.8
313.15	0.0932	1018.8
313.15	0.1931	1037.4
313.15	0.2948	1057.0
313.15	0.3935	1076.8
313.15	0.4987	1098.0
313.15	0.5945	1117.9
313.15	0.7020	1140.6
313.15	0.7949	1160.4
313.15	0.9145	1186.7
313.15	0.9492	1194.9
313.15	1.0000	1206.4

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0437	295.65
0.0966	296.71
0.2056	298.21
0.3047	299.77
0.4022	301.62
0.5075	303.58
0.6174	305.84
0.7161	307.74
0.8111	309.63
0.9003	311.31
0.9485	312.46

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 70 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0431	310.20
0.1232	311.53
0.1949	312.51
0.2993	314.61
0.3945	315.95
0.5001	318.18
0.6101	320.38
0.7125	322.44
0.7947	324.18
0.8986	326.00
0.9515	327.21

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0468	320.72
0.0914	321.68
0.2112	323.42
0.3062	325.45
0.3974	327.13
0.5071	329.01
0.6097	331.45
0.7183	333.63
0.8027	335.11
0.9033	337.41
0.9451	338.32

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0437	295.65
0.0966	296.71
0.2056	298.21
0.3047	299.77
0.4022	301.62
0.5075	303.58
0.6174	305.84
0.7161	307.74
0.8111	309.63
0.9003	311.31
0.9485	312.46

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 70 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0431	310.20
0.1232	311.53
0.1949	312.51
0.2993	314.61
0.3945	315.95
0.5001	318.18
0.6101	320.38
0.7125	322.44
0.7947	324.18
0.8986	326.00
0.9515	327.21

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of Tetrahydrofuran (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0468	320.72
0.0914	321.68
0.2112	323.42
0.3062	325.45
0.3974	327.13
0.5071	329.01
0.6097	331.45
0.7183	333.63
0.8027	335.11
0.9033	337.41
0.9451	338.32

Sources

• Study of isobaric vapour liquid equilibrium of some cyclic ethers with 1-chloropropane: Experimental results and SAFT-VR modelling
• Phase equilibrium and thermophysical properties of mixtures containing a cyclic ether and 1-chloropropane