Mixture of Ethane, fluoro- + Benzene, hexadecyl-

Excel

Ethane, fluoro-

Name
Ethane, fluoro-
InChI
InChI=1S/C2H5F/c1-2-3/h2H2,1H3
InChI Key
UHCBBWUQDAVSMS-UHFFFAOYSA-N
Formula
C2H5F
SMILES
CCF
Mol. Weight (g/mol)
48.06
CAS
353-36-6

Benzene, hexadecyl-

Name
Benzene, hexadecyl-
InChI
InChI=1S/C22H38/c1-2-3-4-5-6-7-8-9-10-11-12-13-14-16-19-22-20-17-15-18-21-22/h15,17-18,20-21H,2-14,16,19H2,1H3
InChI Key
DEQLTFPCJRGSHW-UHFFFAOYSA-N
Formula
C22H38
SMILES
CCCCCCCCCCCCCCCCc1ccccc1
Mol. Weight (g/mol)
302.54
CAS
1459-09-2
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. Pvap - Vapor or sublimation pressure, kPa (2)

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mass fraction of Ethane, fluoro- (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
348.15 0.1245 1124.03
338.15 0.1262 1016.05
328.15 0.1282 902.14
318.15 0.1310 785.75
308.15 0.1326 657.36
298.15 0.1339 534.09
288.15 0.1350 424.20
278.15 0.1379 329.07
338.15 0.1675 1223.31
348.15 0.1697 1395.64
328.15 0.1728 1084.33
318.15 0.2273 1057.72
308.15 0.2296 867.98
298.15 0.2315 713.21
288.15 0.2331 561.04
278.15 0.2361 416.35
348.15 0.2788 1873.70
338.15 0.2792 1610.92
328.15 0.2818 1373.55
318.15 0.2828 1152.20
308.15 0.2868 980.21
298.15 0.2889 777.11
288.15 0.2919 598.86
348.15 0.3955 2213.81
338.15 0.3983 1866.75
328.15 0.4006 1555.79
318.15 0.4042 1281.66
308.15 0.4075 1045.96
298.15 0.4093 835.21
288.15 0.4107 646.16
278.15 0.4118 490.06
348.15 0.4806 2395.70
338.15 0.4820 1994.86
328.15 0.4860 1645.58
318.15 0.4871 1338.70
308.15 0.4897 1069.28
298.15 0.4942 881.54
288.15 0.4955 672.21
278.15 0.4966 504.55
348.15 0.5277 2479.92
318.15 0.5343 1365.21
348.15 0.6071 2601.82
338.15 0.6127 2146.14
328.15 0.6171 1748.99
318.15 0.6207 1406.83
308.15 0.6264 1143.21
298.15 0.6283 908.62
288.15 0.6293 691.87
278.15 0.6300 509.70
348.15 0.7117 2733.07
338.15 0.7188 2241.02
328.15 0.7223 1814.21
318.15 0.7253 1449.69
308.15 0.7283 1166.04
298.15 0.7310 914.51
288.15 0.7318 692.54
278.15 0.7324 510.18
348.15 0.8406 2861.94
338.15 0.8437 2331.87
328.15 0.8461 1878.57
318.15 0.8477 1493.69
308.15 0.8494 1179.65
298.15 0.8505 918.84
288.15 0.8509 693.80
278.15 0.8512 511.45
348.15 0.8912 2905.03
338.15 0.8937 2363.51
328.15 0.8956 1901.57
318.15 0.8971 1510.18
308.15 0.8985 1197.46
298.15 0.8992 921.29
288.15 0.8994 695.02
278.15 0.8996 512.37

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mass fraction of Ethane, fluoro- (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
348.15 0.1245 1124.03
338.15 0.1262 1016.05
328.15 0.1282 902.14
318.15 0.1310 785.75
308.15 0.1326 657.36
298.15 0.1339 534.09
288.15 0.1350 424.20
278.15 0.1379 329.07
338.15 0.1675 1223.31
348.15 0.1697 1395.64
328.15 0.1728 1084.33
318.15 0.2273 1057.72
308.15 0.2296 867.98
298.15 0.2315 713.21
288.15 0.2331 561.04
278.15 0.2361 416.35
348.15 0.2788 1873.70
338.15 0.2792 1610.92
328.15 0.2818 1373.55
318.15 0.2828 1152.20
308.15 0.2868 980.21
298.15 0.2889 777.11
288.15 0.2919 598.86
348.15 0.3955 2213.81
338.15 0.3983 1866.75
328.15 0.4006 1555.79
318.15 0.4042 1281.66
308.15 0.4075 1045.96
298.15 0.4093 835.21
288.15 0.4107 646.16
278.15 0.4118 490.06
348.15 0.4806 2395.70
338.15 0.4820 1994.86
328.15 0.4860 1645.58
318.15 0.4871 1338.70
308.15 0.4897 1069.28
298.15 0.4942 881.54
288.15 0.4955 672.21
278.15 0.4966 504.55
348.15 0.5277 2479.92
318.15 0.5343 1365.21
348.15 0.6071 2601.82
338.15 0.6127 2146.14
328.15 0.6171 1748.99
318.15 0.6207 1406.83
308.15 0.6264 1143.21
298.15 0.6283 908.62
288.15 0.6293 691.87
278.15 0.6300 509.70
348.15 0.7117 2733.07
338.15 0.7188 2241.02
328.15 0.7223 1814.21
318.15 0.7253 1449.69
308.15 0.7283 1166.04
298.15 0.7310 914.51
288.15 0.7318 692.54
278.15 0.7324 510.18
348.15 0.8406 2861.94
338.15 0.8437 2331.87
328.15 0.8461 1878.57
318.15 0.8477 1493.69
308.15 0.8494 1179.65
298.15 0.8505 918.84
288.15 0.8509 693.80
278.15 0.8512 511.45
348.15 0.8912 2905.03
338.15 0.8937 2363.51
328.15 0.8956 1901.57
318.15 0.8971 1510.18
308.15 0.8985 1197.46
298.15 0.8992 921.29
288.15 0.8994 695.02
278.15 0.8996 512.37

Sources