Mixture of Ethane, 1,1,1-trifluoro- + Ethane, fluoro-

Datasets

1. Mole fraction (2)
2. P_vap - Vapor or sublimation pressure, kPa (2)
3. ρ_m,l - Amount density, mol/m3 (2)

Mole fraction of Ethane, 1,1,1-trifluoro- (1) [ref]

Fixed		Measured
Mole fraction of Ethane, 1,1,1-trifluoro- (1) - Liquid	Temperature, K - Liquid	Mole fraction of Ethane, 1,1,1-trifluoro- (1) - Gas
0.0178	278.15	0.0181
0.0266	268.15	0.0362
0.0551	263.15	0.0755
0.0699	258.15	0.0829
0.0731	298.15	0.0946
0.0745	293.15	0.0967
0.0760	288.15	0.0982
0.0784	283.15	0.1004
0.0789	303.15	0.0905
0.0808	253.15	0.1120
0.0865	278.15	0.1098
0.0927	273.15	0.1015
0.1187	278.15	0.1447
0.1236	268.15	0.1565
0.1306	263.15	0.1731
0.1530	273.15	0.1778
0.1566	278.15	0.1899
0.1599	303.15	0.1995
0.1697	253.15	0.2315
0.1699	263.15	0.2162
0.1820	293.15	0.2214
0.1850	283.15	0.2294
0.1855	288.15	0.2271
0.1880	298.15	0.2170
0.2068	258.15	0.2544
0.2209	263.15	0.2743
0.2275	273.15	0.2783
0.2289	268.15	0.2827
0.2511	268.15	0.3117
0.2611	303.15	0.3046
0.2653	253.15	0.3277
0.2715	273.15	0.3207
0.2774	278.15	0.3405
0.2907	293.15	0.3377
0.2918	298.15	0.3294
0.2933	258.15	0.3634
0.2944	288.15	0.3449
0.3002	283.15	0.3513
0.3191	263.15	0.3850
0.3749	293.15	0.4249
0.3788	288.15	0.4324
0.3798	278.15	0.4526
0.3816	258.15	0.4415
0.3830	273.15	0.4548
0.3929	268.15	0.4618
0.3956	298.15	0.4113
0.4043	253.15	0.4705
0.4046	283.15	0.4371
0.4168	303.15	0.4521
0.4454	263.15	0.5112
0.4480	298.15	0.4791
0.4517	293.15	0.4896
0.4636	288.15	0.5034
0.4704	273.15	0.5256
0.4749	283.15	0.5140
0.5002	258.15	0.5780
0.5072	263.15	0.5684
0.5319	253.15	0.6105
0.5348	303.15	0.5746
0.5363	268.15	0.6006
0.5640	273.15	0.6307
0.5767	263.15	0.6390
0.5782	298.15	0.6025
0.5883	278.15	0.6247
0.5944	288.15	0.6305
0.6099	293.15	0.6251
0.6408	258.15	0.7061
0.6542	268.15	0.7135
0.6793	303.15	0.6969
0.6997	288.15	0.7297
0.7013	283.15	0.7356
0.7026	278.15	0.7521
0.7032	298.15	0.7154
0.7055	293.15	0.7234
0.7137	253.15	0.7628
0.7216	268.15	0.7732
0.7429	263.15	0.7895
0.7505	303.15	0.8019
0.7557	258.15	0.8027
0.7576	273.15	0.7888
0.7607	253.15	0.8221
0.8002	268.15	0.8412
0.8126	293.15	0.8350
0.8189	288.15	0.8440
0.8204	273.15	0.8712
0.8209	298.15	0.8244
0.8351	283.15	0.8567
0.8433	263.15	0.8738
0.8545	268.15	0.8800
0.8755	253.15	0.9049
0.8758	273.15	0.8998
0.8778	303.15	0.8841
0.8854	293.15	0.8964
0.8877	288.15	0.8983
0.8884	298.15	0.8921
0.8905	283.15	0.9010
0.8906	278.15	0.9180
0.8919	258.15	0.9155
0.9203	268.15	0.9396
0.9242	263.15	0.9393
0.9374	278.15	0.9524
0.9379	258.15	0.9521
0.9422	253.15	0.9586
0.9444	273.15	0.9542
0.9569	303.15	0.9604
0.9623	293.15	0.9662
0.9624	288.15	0.9662
0.9634	298.15	0.9645
0.9653	283.15	0.9677

Mole fraction of Ethane, 1,1,1-trifluoro- (1) [ref]

Fixed		Measured
Mole fraction of Ethane, 1,1,1-trifluoro- (1) - Liquid	Temperature, K - Liquid	Mole fraction of Ethane, 1,1,1-trifluoro- (1) - Gas
0.0178	278.15	0.0181
0.0266	268.15	0.0362
0.0551	263.15	0.0755
0.0699	258.15	0.0829
0.0731	298.15	0.0946
0.0745	293.15	0.0967
0.0760	288.15	0.0982
0.0784	283.15	0.1004
0.0789	303.15	0.0905
0.0808	253.15	0.1120
0.0865	278.15	0.1098
0.0927	273.15	0.1015
0.1187	278.15	0.1447
0.1236	268.15	0.1565
0.1306	263.15	0.1731
0.1530	273.15	0.1778
0.1566	278.15	0.1899
0.1599	303.15	0.1995
0.1697	253.15	0.2315
0.1699	263.15	0.2162
0.1820	293.15	0.2214
0.1850	283.15	0.2294
0.1855	288.15	0.2271
0.1880	298.15	0.2170
0.2068	258.15	0.2544
0.2209	263.15	0.2743
0.2275	273.15	0.2783
0.2289	268.15	0.2827
0.2511	268.15	0.3117
0.2611	303.15	0.3046
0.2653	253.15	0.3277
0.2715	273.15	0.3207
0.2774	278.15	0.3405
0.2907	293.15	0.3377
0.2918	298.15	0.3294
0.2933	258.15	0.3634
0.2944	288.15	0.3449
0.3002	283.15	0.3513
0.3191	263.15	0.3850
0.3749	293.15	0.4249
0.3788	288.15	0.4324
0.3798	278.15	0.4526
0.3816	258.15	0.4415
0.3830	273.15	0.4548
0.3929	268.15	0.4618
0.3956	298.15	0.4113
0.4043	253.15	0.4705
0.4046	283.15	0.4371
0.4168	303.15	0.4521
0.4454	263.15	0.5112
0.4480	298.15	0.4791
0.4517	293.15	0.4896
0.4636	288.15	0.5034
0.4704	273.15	0.5256
0.4749	283.15	0.5140
0.5002	258.15	0.5780
0.5072	263.15	0.5684
0.5319	253.15	0.6105
0.5348	303.15	0.5746
0.5363	268.15	0.6006
0.5640	273.15	0.6307
0.5767	263.15	0.6390
0.5782	298.15	0.6025
0.5883	278.15	0.6247
0.5944	288.15	0.6305
0.6099	293.15	0.6251
0.6408	258.15	0.7061
0.6542	268.15	0.7135
0.6793	303.15	0.6969
0.6997	288.15	0.7297
0.7013	283.15	0.7356
0.7026	278.15	0.7521
0.7032	298.15	0.7154
0.7055	293.15	0.7234
0.7137	253.15	0.7628
0.7216	268.15	0.7732
0.7429	263.15	0.7895
0.7505	303.15	0.8019
0.7557	258.15	0.8027
0.7576	273.15	0.7888
0.7607	253.15	0.8221
0.8002	268.15	0.8412
0.8126	293.15	0.8350
0.8189	288.15	0.8440
0.8204	273.15	0.8712
0.8209	298.15	0.8244
0.8351	283.15	0.8567
0.8433	263.15	0.8738
0.8545	268.15	0.8800
0.8755	253.15	0.9049
0.8758	273.15	0.8998
0.8778	303.15	0.8841
0.8854	293.15	0.8964
0.8877	288.15	0.8983
0.8884	298.15	0.8921
0.8905	283.15	0.9010
0.8906	278.15	0.9180
0.8919	258.15	0.9155
0.9203	268.15	0.9396
0.9242	263.15	0.9393
0.9374	278.15	0.9524
0.9379	258.15	0.9521
0.9422	253.15	0.9586
0.9444	273.15	0.9542
0.9569	303.15	0.9604
0.9623	293.15	0.9662
0.9624	288.15	0.9662
0.9634	298.15	0.9645
0.9653	283.15	0.9677

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethane, 1,1,1-trifluoro- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0178	278.15	520.50
0.0266	268.15	374.50
0.0551	263.15	318.00
0.0699	258.15	265.00
0.0731	298.15	957.30
0.0745	293.15	834.30
0.0760	288.15	721.70
0.0784	283.15	621.50
0.0789	303.15	1086.50
0.0808	253.15	220.30
0.0865	278.15	536.20
0.0927	273.15	442.90
0.1187	278.15	544.60
0.1236	268.15	390.00
0.1306	263.15	330.00
0.1530	273.15	464.60
0.1566	278.15	553.00
0.1599	303.15	1127.90
0.1697	253.15	230.70
0.1699	263.15	333.90
0.1820	293.15	869.80
0.1850	283.15	650.20
0.1855	288.15	754.00
0.1880	298.15	998.40
0.2068	258.15	279.10
0.2209	263.15	341.40
0.2275	273.15	482.10
0.2289	268.15	410.80
0.2511	268.15	417.50
0.2611	303.15	1178.90
0.2653	253.15	239.90
0.2715	273.15	488.60
0.2774	278.15	585.50
0.2907	293.15	906.20
0.2918	298.15	1039.80
0.2933	258.15	293.90
0.2944	288.15	787.00
0.3002	283.15	678.90
0.3191	263.15	356.50
0.3749	293.15	934.50
0.3788	288.15	810.20
0.3798	278.15	603.80
0.3816	258.15	303.40
0.3830	273.15	514.40
0.3929	268.15	436.40
0.3956	298.15	1068.50
0.4043	253.15	253.80
0.4046	283.15	708.80
0.4168	303.15	1236.00
0.4454	263.15	373.00
0.4480	298.15	1093.90
0.4517	293.15	956.80
0.4636	288.15	832.90
0.4704	273.15	525.40
0.4749	283.15	720.20
0.5002	258.15	319.70
0.5072	263.15	380.40
0.5319	253.15	268.10
0.5348	303.15	1292.20
0.5363	268.15	460.00
0.5640	273.15	544.90
0.5767	263.15	390.30
0.5782	298.15	1139.90
0.5883	278.15	642.00
0.5944	288.15	865.80
0.6099	293.15	995.70
0.6408	258.15	334.50
0.6542	268.15	479.90
0.6793	303.15	1335.80
0.6997	288.15	893.20
0.7013	283.15	772.90
0.7026	278.15	667.20
0.7032	298.15	1173.80
0.7055	293.15	1025.90
0.7137	253.15	284.60
0.7216	268.15	488.30
0.7429	263.15	413.20
0.7505	303.15	1368.50
0.7557	258.15	348.00
0.7576	273.15	575.80
0.7607	253.15	291.20
0.8002	268.15	500.80
0.8126	293.15	1061.40
0.8189	288.15	924.30
0.8204	273.15	593.80
0.8209	298.15	1213.20
0.8351	283.15	800.80
0.8433	263.15	426.10
0.8545	268.15	509.70
0.8755	253.15	300.90
0.8758	273.15	600.70
0.8778	303.15	1398.00
0.8854	293.15	1076.40
0.8877	288.15	937.50
0.8884	298.15	1230.10
0.8905	283.15	812.90
0.8906	278.15	706.60
0.8919	258.15	363.10
0.9203	268.15	517.80
0.9242	263.15	436.50
0.9374	278.15	712.90
0.9379	258.15	367.90
0.9422	253.15	307.80
0.9444	273.15	611.70
0.9569	303.15	1420.70
0.9623	293.15	1095.50
0.9624	288.15	954.50
0.9634	298.15	1251.30
0.9653	283.15	826.30

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethane, 1,1,1-trifluoro- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0178	278.15	520.50
0.0266	268.15	374.50
0.0551	263.15	318.00
0.0699	258.15	265.00
0.0731	298.15	957.30
0.0745	293.15	834.30
0.0760	288.15	721.70
0.0784	283.15	621.50
0.0789	303.15	1086.50
0.0808	253.15	220.30
0.0865	278.15	536.20
0.0927	273.15	442.90
0.1187	278.15	544.60
0.1236	268.15	390.00
0.1306	263.15	330.00
0.1530	273.15	464.60
0.1566	278.15	553.00
0.1599	303.15	1127.90
0.1697	253.15	230.70
0.1699	263.15	333.90
0.1820	293.15	869.80
0.1850	283.15	650.20
0.1855	288.15	754.00
0.1880	298.15	998.40
0.2068	258.15	279.10
0.2209	263.15	341.40
0.2275	273.15	482.10
0.2289	268.15	410.80
0.2511	268.15	417.50
0.2611	303.15	1178.90
0.2653	253.15	239.90
0.2715	273.15	488.60
0.2774	278.15	585.50
0.2907	293.15	906.20
0.2918	298.15	1039.80
0.2933	258.15	293.90
0.2944	288.15	787.00
0.3002	283.15	678.90
0.3191	263.15	356.50
0.3749	293.15	934.50
0.3788	288.15	810.20
0.3798	278.15	603.80
0.3816	258.15	303.40
0.3830	273.15	514.40
0.3929	268.15	436.40
0.3956	298.15	1068.50
0.4043	253.15	253.80
0.4046	283.15	708.80
0.4168	303.15	1236.00
0.4454	263.15	373.00
0.4480	298.15	1093.90
0.4517	293.15	956.80
0.4636	288.15	832.90
0.4704	273.15	525.40
0.4749	283.15	720.20
0.5002	258.15	319.70
0.5072	263.15	380.40
0.5319	253.15	268.10
0.5348	303.15	1292.20
0.5363	268.15	460.00
0.5640	273.15	544.90
0.5767	263.15	390.30
0.5782	298.15	1139.90
0.5883	278.15	642.00
0.5944	288.15	865.80
0.6099	293.15	995.70
0.6408	258.15	334.50
0.6542	268.15	479.90
0.6793	303.15	1335.80
0.6997	288.15	893.20
0.7013	283.15	772.90
0.7026	278.15	667.20
0.7032	298.15	1173.80
0.7055	293.15	1025.90
0.7137	253.15	284.60
0.7216	268.15	488.30
0.7429	263.15	413.20
0.7505	303.15	1368.50
0.7557	258.15	348.00
0.7576	273.15	575.80
0.7607	253.15	291.20
0.8002	268.15	500.80
0.8126	293.15	1061.40
0.8189	288.15	924.30
0.8204	273.15	593.80
0.8209	298.15	1213.20
0.8351	283.15	800.80
0.8433	263.15	426.10
0.8545	268.15	509.70
0.8755	253.15	300.90
0.8758	273.15	600.70
0.8778	303.15	1398.00
0.8854	293.15	1076.40
0.8877	288.15	937.50
0.8884	298.15	1230.10
0.8905	283.15	812.90
0.8906	278.15	706.60
0.8919	258.15	363.10
0.9203	268.15	517.80
0.9242	263.15	436.50
0.9374	278.15	712.90
0.9379	258.15	367.90
0.9422	253.15	307.80
0.9444	273.15	611.70
0.9569	303.15	1420.70
0.9623	293.15	1095.50
0.9624	288.15	954.50
0.9634	298.15	1251.30
0.9653	283.15	826.30

Amount density, mol/m3 [ref]

Fixed			Measured
Temperature, K - Fluid (supercritical or subcritical phases)	Pressure, kPa - Fluid (supercritical or subcritical phases)	Mole fraction of Ethane, fluoro- (2) - Fluid (supercritical or subcritical phases)	Amount density, mol/m3 - Fluid (supercritical or subcritical phases)
308.14	1077.30	0.5513	516.9
313.18	1105.60	0.5513	516.7
313.19	1289.20	0.4404	628.7
313.19	1327.70	0.7454	655.7
318.18	1533.10	0.5398	766.4
318.19	1324.30	0.4404	628.5
318.19	1133.10	0.5513	516.6
318.20	1367.20	0.7454	655.5
323.13	1824.00	0.6821	952.0
323.18	1578.30	0.5398	766.2
323.19	1161.00	0.5513	516.5
323.19	1359.80	0.4404	628.4
323.19	1405.10	0.7454	655.3
328.15	1886.90	0.6821	951.8
328.18	1393.90	0.4404	628.2
328.18	1187.60	0.5513	516.3
328.19	1622.80	0.5398	766.0
328.19	1441.80	0.7454	655.2
333.16	1945.30	0.6821	951.5
333.18	1665.60	0.5398	765.8
333.18	1214.00	0.5513	516.2
333.18	1477.40	0.7454	655.0
333.19	1427.20	0.4404	628.0
338.17	2722.90	0.3852	1609.1
338.17	2001.20	0.6821	951.3
338.18	1708.40	0.5398	765.6
338.18	1460.70	0.4404	627.9
338.19	1512.30	0.7454	654.8
338.19	1240.70	0.5513	516.1
343.16	2056.00	0.6821	951.1
343.17	2832.10	0.3852	1608.7
343.18	1750.50	0.5398	765.4
343.18	1266.60	0.5513	515.9
343.18	1547.00	0.7454	654.7
343.19	1493.60	0.4404	627.7
348.17	1791.60	0.5398	765.2
348.17	2109.80	0.6821	950.8
348.17	2936.90	0.3852	1608.3
348.18	3257.10	0.4746	2022.4
348.18	1526.30	0.4404	627.6
348.18	1292.80	0.5513	515.8
348.18	1581.70	0.7454	654.5
353.16	3291.20	0.8703	1938.1
353.16	2163.40	0.6821	950.6
353.17	3040.30	0.3852	1607.9
353.18	1832.60	0.5398	765.0
353.18	3397.30	0.4746	2021.8
353.19	1615.20	0.7454	654.3
353.19	1318.20	0.5513	515.7
353.19	1558.90	0.4404	627.4
358.18	1343.40	0.5513	515.6
358.18	1591.00	0.4404	627.2
358.19	1873.10	0.5398	764.9
358.20	3533.90	0.4746	2021.3
358.20	3141.70	0.3852	1607.5
358.22	2215.70	0.6821	950.3
358.22	1648.40	0.7454	654.2
358.22	3436.50	0.8703	1937.6
363.16	1913.50	0.5398	764.7
363.18	1682.40	0.7454	654.0
363.18	3667.50	0.4746	2020.8
363.18	3241.70	0.3852	1607.1
363.19	2268.40	0.6821	950.1
363.20	3565.90	0.8703	1937.1
363.22	1369.30	0.5513	515.4
363.23	1622.90	0.4404	627.1
368.15	1953.40	0.5398	764.5
368.16	3799.10	0.4746	2020.3
368.16	3340.70	0.3852	1606.7
368.17	2319.90	0.6821	949.9
368.17	1654.90	0.4404	626.9
368.17	1394.50	0.5513	515.3
368.18	3691.10	0.8703	1936.6
368.18	1715.40	0.7454	653.8
373.15	1419.90	0.5513	515.2
373.15	1748.10	0.7454	653.7
373.16	1685.90	0.4404	626.8
373.17	3815.50	0.8703	1936.1
373.17	3439.40	0.3852	1606.3
373.18	1993.60	0.5398	764.3
373.19	3930.30	0.4746	2019.8
373.19	2372.30	0.6821	949.6
378.13	2422.80	0.6821	949.4
378.14	3937.30	0.8703	1935.6
378.15	2032.80	0.5398	764.1
378.15	1444.90	0.5513	515.0
378.17	3535.80	0.3852	1605.9
378.17	4058.60	0.4746	2019.3
378.23	1718.00	0.4404	626.6
378.23	1782.00	0.7454	653.5
383.17	2472.80	0.6821	949.1
383.18	4057.70	0.8703	1935.1
383.20	1469.90	0.5513	514.9
383.21	1749.40	0.4404	626.4
383.21	1814.60	0.7454	653.3
383.21	2072.70	0.5398	763.9
383.23	3632.60	0.3852	1605.4
383.24	4187.70	0.4746	2018.8
388.15	4176.40	0.8703	1934.6
388.16	2522.70	0.6821	948.9
388.19	2112.00	0.5398	763.7
388.19	1780.20	0.4404	626.3
388.20	1846.90	0.7454	653.2
388.21	1495.60	0.5513	514.8
388.22	4313.60	0.4746	2018.2
388.22	3727.90	0.3852	1605.0
393.18	1878.70	0.7454	653.0
393.18	1519.90	0.5513	514.6
393.18	1810.70	0.4404	626.1
393.20	4437.70	0.4746	2017.7
393.20	3821.60	0.3852	1604.6
393.21	2151.20	0.5398	763.5
393.22	2573.50	0.6821	948.6
393.23	4296.60	0.8703	1934.1
398.16	1841.60	0.4404	626.0
398.16	1544.00	0.5513	514.5
398.16	1910.50	0.7454	652.8
398.17	2189.00	0.5398	763.3
398.19	4561.50	0.4746	2017.2
398.19	2622.50	0.6821	948.4
398.20	3915.50	0.3852	1604.2
398.22	4412.30	0.8703	1933.6
403.14	1568.20	0.5513	514.4
403.15	2227.50	0.5398	763.1
403.17	1872.40	0.4404	625.8
403.18	4684.30	0.4746	2016.7
403.18	4008.20	0.3852	1603.8
403.18	2671.90	0.6821	948.2
403.20	4528.10	0.8703	1933.1
403.20	1942.90	0.7454	652.7

Amount density, mol/m3 [ref]

Fixed			Measured
Temperature, K - Fluid (supercritical or subcritical phases)	Pressure, kPa - Fluid (supercritical or subcritical phases)	Mole fraction of Ethane, fluoro- (2) - Fluid (supercritical or subcritical phases)	Amount density, mol/m3 - Fluid (supercritical or subcritical phases)
308.14	1077.30	0.5513	516.9
313.18	1105.60	0.5513	516.7
313.19	1289.20	0.4404	628.7
313.19	1327.70	0.7454	655.7
318.18	1533.10	0.5398	766.4
318.19	1324.30	0.4404	628.5
318.19	1133.10	0.5513	516.6
318.20	1367.20	0.7454	655.5
323.13	1824.00	0.6821	952.0
323.18	1578.30	0.5398	766.2
323.19	1161.00	0.5513	516.5
323.19	1359.80	0.4404	628.4
323.19	1405.10	0.7454	655.3
328.15	1886.90	0.6821	951.8
328.18	1393.90	0.4404	628.2
328.18	1187.60	0.5513	516.3
328.19	1622.80	0.5398	766.0
328.19	1441.80	0.7454	655.2
333.16	1945.30	0.6821	951.5
333.18	1665.60	0.5398	765.8
333.18	1214.00	0.5513	516.2
333.18	1477.40	0.7454	655.0
333.19	1427.20	0.4404	628.0
338.17	2722.90	0.3852	1609.1
338.17	2001.20	0.6821	951.3
338.18	1708.40	0.5398	765.6
338.18	1460.70	0.4404	627.9
338.19	1512.30	0.7454	654.8
338.19	1240.70	0.5513	516.1
343.16	2056.00	0.6821	951.1
343.17	2832.10	0.3852	1608.7
343.18	1750.50	0.5398	765.4
343.18	1266.60	0.5513	515.9
343.18	1547.00	0.7454	654.7
343.19	1493.60	0.4404	627.7
348.17	1791.60	0.5398	765.2
348.17	2109.80	0.6821	950.8
348.17	2936.90	0.3852	1608.3
348.18	3257.10	0.4746	2022.4
348.18	1526.30	0.4404	627.6
348.18	1292.80	0.5513	515.8
348.18	1581.70	0.7454	654.5
353.16	3291.20	0.8703	1938.1
353.16	2163.40	0.6821	950.6
353.17	3040.30	0.3852	1607.9
353.18	1832.60	0.5398	765.0
353.18	3397.30	0.4746	2021.8
353.19	1615.20	0.7454	654.3
353.19	1318.20	0.5513	515.7
353.19	1558.90	0.4404	627.4
358.18	1343.40	0.5513	515.6
358.18	1591.00	0.4404	627.2
358.19	1873.10	0.5398	764.9
358.20	3533.90	0.4746	2021.3
358.20	3141.70	0.3852	1607.5
358.22	2215.70	0.6821	950.3
358.22	1648.40	0.7454	654.2
358.22	3436.50	0.8703	1937.6
363.16	1913.50	0.5398	764.7
363.18	1682.40	0.7454	654.0
363.18	3667.50	0.4746	2020.8
363.18	3241.70	0.3852	1607.1
363.19	2268.40	0.6821	950.1
363.20	3565.90	0.8703	1937.1
363.22	1369.30	0.5513	515.4
363.23	1622.90	0.4404	627.1
368.15	1953.40	0.5398	764.5
368.16	3799.10	0.4746	2020.3
368.16	3340.70	0.3852	1606.7
368.17	2319.90	0.6821	949.9
368.17	1654.90	0.4404	626.9
368.17	1394.50	0.5513	515.3
368.18	3691.10	0.8703	1936.6
368.18	1715.40	0.7454	653.8
373.15	1419.90	0.5513	515.2
373.15	1748.10	0.7454	653.7
373.16	1685.90	0.4404	626.8
373.17	3815.50	0.8703	1936.1
373.17	3439.40	0.3852	1606.3
373.18	1993.60	0.5398	764.3
373.19	3930.30	0.4746	2019.8
373.19	2372.30	0.6821	949.6
378.13	2422.80	0.6821	949.4
378.14	3937.30	0.8703	1935.6
378.15	2032.80	0.5398	764.1
378.15	1444.90	0.5513	515.0
378.17	3535.80	0.3852	1605.9
378.17	4058.60	0.4746	2019.3
378.23	1718.00	0.4404	626.6
378.23	1782.00	0.7454	653.5
383.17	2472.80	0.6821	949.1
383.18	4057.70	0.8703	1935.1
383.20	1469.90	0.5513	514.9
383.21	1749.40	0.4404	626.4
383.21	1814.60	0.7454	653.3
383.21	2072.70	0.5398	763.9
383.23	3632.60	0.3852	1605.4
383.24	4187.70	0.4746	2018.8
388.15	4176.40	0.8703	1934.6
388.16	2522.70	0.6821	948.9
388.19	2112.00	0.5398	763.7
388.19	1780.20	0.4404	626.3
388.20	1846.90	0.7454	653.2
388.21	1495.60	0.5513	514.8
388.22	4313.60	0.4746	2018.2
388.22	3727.90	0.3852	1605.0
393.18	1878.70	0.7454	653.0
393.18	1519.90	0.5513	514.6
393.18	1810.70	0.4404	626.1
393.20	4437.70	0.4746	2017.7
393.20	3821.60	0.3852	1604.6
393.21	2151.20	0.5398	763.5
393.22	2573.50	0.6821	948.6
393.23	4296.60	0.8703	1934.1
398.16	1841.60	0.4404	626.0
398.16	1544.00	0.5513	514.5
398.16	1910.50	0.7454	652.8
398.17	2189.00	0.5398	763.3
398.19	4561.50	0.4746	2017.2
398.19	2622.50	0.6821	948.4
398.20	3915.50	0.3852	1604.2
398.22	4412.30	0.8703	1933.6
403.14	1568.20	0.5513	514.4
403.15	2227.50	0.5398	763.1
403.17	1872.40	0.4404	625.8
403.18	4684.30	0.4746	2016.7
403.18	4008.20	0.3852	1603.8
403.18	2671.90	0.6821	948.2
403.20	4528.10	0.8703	1933.1
403.20	1942.90	0.7454	652.7

Sources

• Gas phase PVTx properties for binary mixtures of HFC-161 and HFC-143a
• Isothermal Vapor-Liquid Equilibrium Data for the Binary Mixture Trifluoroethane (HFC-143a) + Ethyl Fluoride (HFC-161) over the Temperature Range (253.15 to 303.15) K