Ethane, fluoro- + Ethane, pentafluoro-

Datasets

Mole fraction (2)
P_vap - Vapor or sublimation pressure, kPa (2)
ρ_m,g - Amount density, mol/m3 (2)

Mole fraction of Ethane, pentafluoro- (2) [ref]

Fixed		Measured
Mole fraction of Ethane, pentafluoro- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethane, pentafluoro- (2) - Gas
0.0000	265.15	0.0000
0.0000	275.15	0.0000
0.0000	283.15	0.0000
0.0000	293.15	0.0000
0.0000	303.15	0.0000
0.0000	313.15	0.0000
0.1165	283.15	0.1577
0.1437	283.15	0.1938
0.2370	283.15	0.3131
0.3229	283.15	0.4156
0.3234	265.15	0.4248
0.3293	293.15	0.4234
0.4020	265.15	0.5227
0.4254	265.15	0.5498
0.4452	313.15	0.4830
0.4516	275.15	0.5712
0.4527	303.15	0.5030
0.4660	283.15	0.5776
0.5154	313.15	0.5558
0.5383	293.15	0.6383
0.5438	283.15	0.6520
0.5511	275.15	0.6706
0.5563	265.15	0.6703
0.5591	303.15	0.6045
0.5620	293.15	0.6609
0.5844	313.15	0.6161
0.5999	275.15	0.7124
0.6053	293.15	0.7060
0.6068	303.15	0.6444
0.6332	283.15	0.7311
0.6592	313.15	0.6845
0.6740	265.15	0.7743
0.6806	283.15	0.7786
0.6859	293.15	0.7689
0.7184	313.15	0.7471
0.7236	313.15	0.7548
0.7257	265.15	0.8022
0.7289	303.15	0.7536
0.7319	275.15	0.8134
0.7348	283.15	0.8140
0.7551	293.15	0.8128
0.7558	283.15	0.8323
0.7590	265.15	0.8232
0.7596	303.15	0.7839
0.7724	275.15	0.8404
0.7749	313.15	0.8043
0.7832	303.15	0.8039
0.7856	293.15	0.8328
0.7936	265.15	0.8507
0.7966	293.15	0.8409
0.7968	303.15	0.8214
0.7990	283.15	0.8613
0.8075	275.15	0.8633
0.8094	293.15	0.8596
0.8129	265.15	0.8616
0.8202	265.15	0.8744
0.8260	275.15	0.8759
0.8320	293.15	0.8730
0.8322	313.15	0.8529
0.8335	283.15	0.8849
0.8385	275.15	0.8840
0.8451	303.15	0.8595
0.8464	293.15	0.8818
0.8551	275.15	0.8889
0.8575	265.15	0.8873
0.8602	303.15	0.8738
0.8695	313.15	0.8900
0.8800	275.15	0.9196
0.8837	283.15	0.9191
1.0000	265.15	1.0000
1.0000	275.15	1.0000
1.0000	283.15	1.0000
1.0000	293.15	1.0000
1.0000	303.15	1.0000
1.0000	313.15	1.0000

Mole fraction of Ethane, pentafluoro- (2) [ref]

Fixed		Measured
Mole fraction of Ethane, pentafluoro- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethane, pentafluoro- (2) - Gas
0.0000	265.15	0.0000
0.0000	275.15	0.0000
0.0000	283.15	0.0000
0.0000	293.15	0.0000
0.0000	303.15	0.0000
0.0000	313.15	0.0000
0.1165	283.15	0.1577
0.1437	283.15	0.1938
0.2370	283.15	0.3131
0.3229	283.15	0.4156
0.3234	265.15	0.4248
0.3293	293.15	0.4234
0.4020	265.15	0.5227
0.4254	265.15	0.5498
0.4452	313.15	0.4830
0.4516	275.15	0.5712
0.4527	303.15	0.5030
0.4660	283.15	0.5776
0.5154	313.15	0.5558
0.5383	293.15	0.6383
0.5438	283.15	0.6520
0.5511	275.15	0.6706
0.5563	265.15	0.6703
0.5591	303.15	0.6045
0.5620	293.15	0.6609
0.5844	313.15	0.6161
0.5999	275.15	0.7124
0.6053	293.15	0.7060
0.6068	303.15	0.6444
0.6332	283.15	0.7311
0.6592	313.15	0.6845
0.6740	265.15	0.7743
0.6806	283.15	0.7786
0.6859	293.15	0.7689
0.7184	313.15	0.7471
0.7236	313.15	0.7548
0.7257	265.15	0.8022
0.7289	303.15	0.7536
0.7319	275.15	0.8134
0.7348	283.15	0.8140
0.7551	293.15	0.8128
0.7558	283.15	0.8323
0.7590	265.15	0.8232
0.7596	303.15	0.7839
0.7724	275.15	0.8404
0.7749	313.15	0.8043
0.7832	303.15	0.8039
0.7856	293.15	0.8328
0.7936	265.15	0.8507
0.7966	293.15	0.8409
0.7968	303.15	0.8214
0.7990	283.15	0.8613
0.8075	275.15	0.8633
0.8094	293.15	0.8596
0.8129	265.15	0.8616
0.8202	265.15	0.8744
0.8260	275.15	0.8759
0.8320	293.15	0.8730
0.8322	313.15	0.8529
0.8335	283.15	0.8849
0.8385	275.15	0.8840
0.8451	303.15	0.8595
0.8464	293.15	0.8818
0.8551	275.15	0.8889
0.8575	265.15	0.8873
0.8602	303.15	0.8738
0.8695	313.15	0.8900
0.8800	275.15	0.9196
0.8837	283.15	0.9191
1.0000	265.15	1.0000
1.0000	275.15	1.0000
1.0000	283.15	1.0000
1.0000	293.15	1.0000
1.0000	303.15	1.0000
1.0000	313.15	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethane, pentafluoro- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	265.15	336.00
0.0000	275.15	468.90
0.0000	283.15	602.90
0.0000	293.15	808.20
0.0000	303.15	1051.40
0.0000	313.15	1348.60
0.1165	283.15	632.50
0.1437	283.15	636.50
0.2370	283.15	663.70
0.3229	283.15	690.50
0.3234	265.15	392.80
0.3293	293.15	955.90
0.4020	265.15	410.90
0.4254	265.15	414.70
0.4452	313.15	1812.60
0.4516	275.15	578.80
0.4527	303.15	1393.00
0.4660	283.15	737.40
0.5154	313.15	1833.60
0.5383	293.15	1038.70
0.5438	283.15	766.60
0.5511	275.15	599.90
0.5563	265.15	438.80
0.5591	303.15	1422.10
0.5620	293.15	1053.30
0.5844	313.15	1857.30
0.5999	275.15	624.60
0.6053	293.15	1079.70
0.6068	303.15	1442.60
0.6332	283.15	809.10
0.6592	313.15	1872.70
0.6740	265.15	461.70
0.6806	283.15	812.80
0.6859	293.15	1093.30
0.7184	313.15	1899.90
0.7236	313.15	1907.30
0.7257	265.15	471.65
0.7289	303.15	1487.80
0.7319	275.15	651.00
0.7348	283.15	830.50
0.7551	293.15	1118.90
0.7558	283.15	839.80
0.7590	265.15	480.50
0.7596	303.15	1491.90
0.7724	275.15	659.40
0.7749	313.15	1917.00
0.7832	303.15	1506.90
0.7856	293.15	1123.40
0.7936	265.15	485.10
0.7966	293.15	1133.60
0.7968	303.15	1514.70
0.7990	283.15	849.20
0.8075	275.15	666.30
0.8094	293.15	1134.40
0.8129	265.15	488.70
0.8202	265.15	495.80
0.8260	275.15	679.00
0.8320	293.15	1140.10
0.8322	313.15	1928.00
0.8335	283.15	863.57
0.8385	275.15	681.60
0.8451	303.15	1529.30
0.8464	293.15	1156.10
0.8551	275.15	690.80
0.8575	265.15	502.30
0.8602	303.15	1539.30
0.8695	313.15	1944.00
0.8800	275.15	702.40
0.8837	283.15	880.93
1.0000	265.15	517.00
1.0000	275.15	714.30
1.0000	283.15	908.80
1.0000	293.15	1205.00
1.0000	303.15	1567.00
1.0000	313.15	2006.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethane, pentafluoro- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	265.15	336.00
0.0000	275.15	468.90
0.0000	283.15	602.90
0.0000	293.15	808.20
0.0000	303.15	1051.40
0.0000	313.15	1348.60
0.1165	283.15	632.50
0.1437	283.15	636.50
0.2370	283.15	663.70
0.3229	283.15	690.50
0.3234	265.15	392.80
0.3293	293.15	955.90
0.4020	265.15	410.90
0.4254	265.15	414.70
0.4452	313.15	1812.60
0.4516	275.15	578.80
0.4527	303.15	1393.00
0.4660	283.15	737.40
0.5154	313.15	1833.60
0.5383	293.15	1038.70
0.5438	283.15	766.60
0.5511	275.15	599.90
0.5563	265.15	438.80
0.5591	303.15	1422.10
0.5620	293.15	1053.30
0.5844	313.15	1857.30
0.5999	275.15	624.60
0.6053	293.15	1079.70
0.6068	303.15	1442.60
0.6332	283.15	809.10
0.6592	313.15	1872.70
0.6740	265.15	461.70
0.6806	283.15	812.80
0.6859	293.15	1093.30
0.7184	313.15	1899.90
0.7236	313.15	1907.30
0.7257	265.15	471.65
0.7289	303.15	1487.80
0.7319	275.15	651.00
0.7348	283.15	830.50
0.7551	293.15	1118.90
0.7558	283.15	839.80
0.7590	265.15	480.50
0.7596	303.15	1491.90
0.7724	275.15	659.40
0.7749	313.15	1917.00
0.7832	303.15	1506.90
0.7856	293.15	1123.40
0.7936	265.15	485.10
0.7966	293.15	1133.60
0.7968	303.15	1514.70
0.7990	283.15	849.20
0.8075	275.15	666.30
0.8094	293.15	1134.40
0.8129	265.15	488.70
0.8202	265.15	495.80
0.8260	275.15	679.00
0.8320	293.15	1140.10
0.8322	313.15	1928.00
0.8335	283.15	863.57
0.8385	275.15	681.60
0.8451	303.15	1529.30
0.8464	293.15	1156.10
0.8551	275.15	690.80
0.8575	265.15	502.30
0.8602	303.15	1539.30
0.8695	313.15	1944.00
0.8800	275.15	702.40
0.8837	283.15	880.93
1.0000	265.15	517.00
1.0000	275.15	714.30
1.0000	283.15	908.80
1.0000	293.15	1205.00
1.0000	303.15	1567.00
1.0000	313.15	2006.00

Amount density, mol/m3 [ref]

Fixed			Measured
Temperature, K - Gas	Pressure, kPa - Gas	Mole fraction of Ethane, fluoro- (1) - Gas	Amount density, mol/m3 - Gas
308.15	1127.10	0.8452	556.2
308.16	1131.90	0.6948	561.3
313.15	1084.30	0.9061	504.1
313.16	1166.80	0.6948	561.2
313.17	1165.50	0.8452	556.1
318.15	1112.30	0.9061	504.0
318.16	1197.60	0.8452	556.0
318.16	1199.50	0.6948	561.0
318.16	1464.00	0.5920	737.0
323.15	1229.00	0.8452	555.8
323.15	1509.90	0.5920	736.9
323.15	1935.50	0.3819	1073.3
323.16	1139.40	0.9061	503.8
323.16	1231.10	0.6948	560.9
324.15	1913.60	0.4334	1057.2
325.16	1921.60	0.4146	1039.3
328.14	1963.80	0.4146	1039.2
328.15	1166.20	0.9061	503.7
328.15	1259.20	0.8452	555.7
328.15	1971.10	0.4334	1057.0
328.15	2008.30	0.3819	1073.1
328.16	1262.20	0.6948	560.8
328.16	1553.90	0.5920	736.7
331.14	2011.70	0.4334	1056.8
333.14	2028.60	0.4146	1038.9
333.14	1192.30	0.9061	503.6
333.14	2077.40	0.3819	1072.8
333.15	2038.70	0.4334	1056.7
333.15	1288.90	0.8452	555.5
333.15	1596.90	0.5920	736.5
333.15	1292.60	0.6948	560.6
335.14	2057.10	0.4146	1038.8
335.15	2104.60	0.3819	1072.7
336.15	2078.20	0.4334	1056.6
337.14	2083.00	0.4146	1038.7
337.15	2131.50	0.3819	1072.6
338.15	1318.00	0.8452	555.4
338.15	1322.70	0.6948	560.5
338.15	1638.80	0.5920	736.3
338.15	1218.40	0.9061	503.5
339.15	2108.90	0.4146	1038.6
339.15	2117.90	0.4334	1056.4
339.16	2158.70	0.3819	1072.5
343.14	2160.10	0.4146	1038.4
343.15	2169.90	0.4334	1056.2
343.15	2211.90	0.3819	1072.3
343.15	1346.80	0.8452	555.3
343.15	1680.40	0.5920	736.1
343.15	1243.90	0.9061	503.3
343.16	1352.20	0.6948	560.3
346.15	2197.50	0.4146	1038.2
348.15	1375.80	0.8452	555.1
348.15	1721.10	0.5920	736.0
348.15	1268.80	0.9061	503.2
348.15	2277.30	0.3819	1072.0
348.16	2233.20	0.4334	1056.0
348.16	1381.50	0.6948	560.2
349.14	2235.30	0.4146	1038.1
352.15	2272.40	0.4146	1037.9
353.14	1410.60	0.6948	560.1
353.15	2341.40	0.3819	1071.7
353.15	1404.00	0.8452	555.0
353.15	1761.90	0.5920	735.8
353.15	1294.10	0.9061	503.1
353.16	2296.10	0.4334	1055.7
355.15	2367.20	0.3819	1071.6
355.15	2309.70	0.4146	1037.8
357.15	2392.70	0.3819	1071.5
357.15	2393.40	0.3819	1071.5
357.16	3883.20	0.5744	2894.1
358.15	2346.50	0.4146	1037.6
358.16	3927.80	0.5744	2893.9
358.19	1432.60	0.8452	554.9
358.20	2358.90	0.4334	1055.4
358.20	1803.30	0.5920	735.6
358.20	1440.10	0.6948	559.9
358.21	1319.40	0.9061	503.0
359.15	3972.90	0.5744	2893.8
359.23	2419.90	0.3819	1071.4
361.16	4061.90	0.5744	2893.5
361.20	2445.00	0.3819	1071.3
363.15	4150.10	0.5744	2893.2
363.17	1460.80	0.8452	554.7
363.17	2419.60	0.4334	1055.2
363.18	1842.40	0.5920	735.4
363.18	1468.70	0.6948	559.8
363.18	2407.00	0.4146	1037.3
364.16	2481.30	0.3819	1071.1
365.14	4236.60	0.5744	2892.9
367.17	4323.80	0.5744	2892.7
368.15	2467.20	0.4146	1037.1
368.15	2480.50	0.4334	1054.9
368.15	1497.60	0.6948	559.7
368.15	1882.50	0.5920	735.2
368.18	1488.90	0.8452	554.6
368.19	2531.70	0.3819	1070.9
369.15	4410.10	0.5744	2892.4
371.20	4498.00	0.5744	2892.1
373.16	2540.60	0.4334	1054.6
373.17	2527.20	0.4146	1036.8
373.18	1921.90	0.5920	735.0
373.18	2593.10	0.3819	1070.7
373.18	4583.30	0.5744	2891.8
373.19	1526.00	0.6948	559.5
378.13	2585.70	0.4146	1036.6
378.15	4793.20	0.5744	2891.1
378.15	1554.10	0.6948	559.4
378.16	2653.90	0.3819	1070.4
378.17	2599.80	0.4334	1054.4
378.19	1960.50	0.5920	734.9
383.17	5003.50	0.5744	2890.4
383.22	2644.00	0.4146	1036.3
383.22	1581.60	0.6948	559.2
383.23	1998.70	0.5920	734.7
383.23	2659.10	0.4334	1054.1
383.26	2715.40	0.3819	1070.1
388.20	1608.80	0.6948	559.1
388.20	2775.10	0.3819	1069.9
388.20	2701.50	0.4146	1036.1
388.21	2716.60	0.4334	1053.9
388.21	2037.20	0.5920	734.5
388.25	5213.40	0.5744	2889.6
393.18	2757.90	0.4146	1035.8
393.19	2074.60	0.5920	734.3
393.19	2834.20	0.3819	1069.6
393.20	1636.30	0.6948	559.0
393.20	2774.10	0.4334	1053.6
393.23	5416.50	0.5744	2888.9

Amount density, mol/m3 [ref]

Fixed			Measured
Temperature, K - Gas	Pressure, kPa - Gas	Mole fraction of Ethane, fluoro- (1) - Gas	Amount density, mol/m3 - Gas
308.15	1127.10	0.8452	556.2
308.16	1131.90	0.6948	561.3
313.15	1084.30	0.9061	504.1
313.16	1166.80	0.6948	561.2
313.17	1165.50	0.8452	556.1
318.15	1112.30	0.9061	504.0
318.16	1197.60	0.8452	556.0
318.16	1199.50	0.6948	561.0
318.16	1464.00	0.5920	737.0
323.15	1229.00	0.8452	555.8
323.15	1509.90	0.5920	736.9
323.15	1935.50	0.3819	1073.3
323.16	1139.40	0.9061	503.8
323.16	1231.10	0.6948	560.9
324.15	1913.60	0.4334	1057.2
325.16	1921.60	0.4146	1039.3
328.14	1963.80	0.4146	1039.2
328.15	1166.20	0.9061	503.7
328.15	1259.20	0.8452	555.7
328.15	1971.10	0.4334	1057.0
328.15	2008.30	0.3819	1073.1
328.16	1262.20	0.6948	560.8
328.16	1553.90	0.5920	736.7
331.14	2011.70	0.4334	1056.8
333.14	2028.60	0.4146	1038.9
333.14	1192.30	0.9061	503.6
333.14	2077.40	0.3819	1072.8
333.15	2038.70	0.4334	1056.7
333.15	1288.90	0.8452	555.5
333.15	1596.90	0.5920	736.5
333.15	1292.60	0.6948	560.6
335.14	2057.10	0.4146	1038.8
335.15	2104.60	0.3819	1072.7
336.15	2078.20	0.4334	1056.6
337.14	2083.00	0.4146	1038.7
337.15	2131.50	0.3819	1072.6
338.15	1318.00	0.8452	555.4
338.15	1322.70	0.6948	560.5
338.15	1638.80	0.5920	736.3
338.15	1218.40	0.9061	503.5
339.15	2108.90	0.4146	1038.6
339.15	2117.90	0.4334	1056.4
339.16	2158.70	0.3819	1072.5
343.14	2160.10	0.4146	1038.4
343.15	2169.90	0.4334	1056.2
343.15	2211.90	0.3819	1072.3
343.15	1346.80	0.8452	555.3
343.15	1680.40	0.5920	736.1
343.15	1243.90	0.9061	503.3
343.16	1352.20	0.6948	560.3
346.15	2197.50	0.4146	1038.2
348.15	1375.80	0.8452	555.1
348.15	1721.10	0.5920	736.0
348.15	1268.80	0.9061	503.2
348.15	2277.30	0.3819	1072.0
348.16	2233.20	0.4334	1056.0
348.16	1381.50	0.6948	560.2
349.14	2235.30	0.4146	1038.1
352.15	2272.40	0.4146	1037.9
353.14	1410.60	0.6948	560.1
353.15	2341.40	0.3819	1071.7
353.15	1404.00	0.8452	555.0
353.15	1761.90	0.5920	735.8
353.15	1294.10	0.9061	503.1
353.16	2296.10	0.4334	1055.7
355.15	2367.20	0.3819	1071.6
355.15	2309.70	0.4146	1037.8
357.15	2392.70	0.3819	1071.5
357.15	2393.40	0.3819	1071.5
357.16	3883.20	0.5744	2894.1
358.15	2346.50	0.4146	1037.6
358.16	3927.80	0.5744	2893.9
358.19	1432.60	0.8452	554.9
358.20	2358.90	0.4334	1055.4
358.20	1803.30	0.5920	735.6
358.20	1440.10	0.6948	559.9
358.21	1319.40	0.9061	503.0
359.15	3972.90	0.5744	2893.8
359.23	2419.90	0.3819	1071.4
361.16	4061.90	0.5744	2893.5
361.20	2445.00	0.3819	1071.3
363.15	4150.10	0.5744	2893.2
363.17	1460.80	0.8452	554.7
363.17	2419.60	0.4334	1055.2
363.18	1842.40	0.5920	735.4
363.18	1468.70	0.6948	559.8
363.18	2407.00	0.4146	1037.3
364.16	2481.30	0.3819	1071.1
365.14	4236.60	0.5744	2892.9
367.17	4323.80	0.5744	2892.7
368.15	2467.20	0.4146	1037.1
368.15	2480.50	0.4334	1054.9
368.15	1497.60	0.6948	559.7
368.15	1882.50	0.5920	735.2
368.18	1488.90	0.8452	554.6
368.19	2531.70	0.3819	1070.9
369.15	4410.10	0.5744	2892.4
371.20	4498.00	0.5744	2892.1
373.16	2540.60	0.4334	1054.6
373.17	2527.20	0.4146	1036.8
373.18	1921.90	0.5920	735.0
373.18	2593.10	0.3819	1070.7
373.18	4583.30	0.5744	2891.8
373.19	1526.00	0.6948	559.5
378.13	2585.70	0.4146	1036.6
378.15	4793.20	0.5744	2891.1
378.15	1554.10	0.6948	559.4
378.16	2653.90	0.3819	1070.4
378.17	2599.80	0.4334	1054.4
378.19	1960.50	0.5920	734.9
383.17	5003.50	0.5744	2890.4
383.22	2644.00	0.4146	1036.3
383.22	1581.60	0.6948	559.2
383.23	1998.70	0.5920	734.7
383.23	2659.10	0.4334	1054.1
383.26	2715.40	0.3819	1070.1
388.20	1608.80	0.6948	559.1
388.20	2775.10	0.3819	1069.9
388.20	2701.50	0.4146	1036.1
388.21	2716.60	0.4334	1053.9
388.21	2037.20	0.5920	734.5
388.25	5213.40	0.5744	2889.6
393.18	2757.90	0.4146	1035.8
393.19	2074.60	0.5920	734.3
393.19	2834.20	0.3819	1069.6
393.20	1636.30	0.6948	559.0
393.20	2774.10	0.4334	1053.6
393.23	5416.50	0.5744	2888.9

Sources

PVTx properties in the gas phase for binary HFC-161/125 system
Isothermal Vapor-Liquid Equilibrium of (Pentafluoroethane + Fluoroethane) at Temperatures between (265.15 and 303.15) K Obtained with a Recirculating Still

Mixture of Ethane, fluoro- + Ethane, pentafluoro-

Datasets

Mole fraction of Ethane, pentafluoro- (2) [ref]

Mole fraction of Ethane, pentafluoro- (2) [ref]

Vapor or sublimation pressure, kPa [ref]

Vapor or sublimation pressure, kPa [ref]

Amount density, mol/m3 [ref]

Amount density, mol/m3 [ref]

Sources