2 0 2007 des men 0 journal Original Deschamps, J. Menz, D.-H. Padua, A. A. H. Gomes, M. F. C. J. Chem. Thermodyn. 2007 2007-07-11 Low pressure solubility and thermodynamics of solvation of oxygen, carbon dioxide, and carbon monoxide in fluorinated liquids Perfluorohexylethane Perfluoromethylcyclohexane Perfluorodimethylcyclohexane Perfluorophenanthrene Perfluorooctane Perfluorodecalin 1-Bromoperfluorooctane Oxygen Carbon dioxide Carbon monoxide Solubility 39 847-854 307346 octadecafluorooctane C8F18 1 Commercial source 1 99.4 3 Stated by supplier 2 Unspecified 423552 1-bromoperfluorooctane C8BrF17 1 Commercial source 1 98.1 3 Stated by supplier 2 Unspecified 306945 perfluorodecalin C10F18 1 Commercial source 1 98.7 3 Stated by supplier 2 Unspecified 355022 cyclohexane, undecafluoro(trifluoromethyl)- C7F14 1 Commercial source 1 97.4 3 Stated by supplier 2 Unspecified 335273 cyclohexane, 1,1,2,2,3,3,4,5,5,6-decafluoro-4,6-bis(trifluoromethyl)- C8F16 1 Commercial source 1 99.2 3 Stated by supplier 2 Unspecified 306912 perfluorophenanthrene C14F24 1 Commercial source 1 93 2 Stated by supplier 2 Unspecified 124389 carbon dioxide CO2 1 Commercial source 1 99.995 5 Stated by supplier 2 None used 630080 carbon monoxide CO 1 Commercial source 1 99.997 5 Stated by supplier 2 None used 7782447 oxygen O2 1 80793175 perfluorohexylethane C8H5F13 1 Commercial source 1 99.99 4 Stated by supplier 2 None used 307346 1 Principal objective of the work HR HR 5/8/2007 1 Mass density, kg/m3 Pycnometric method Liquid Direct value, X Liquid Gas 1 Temperature, K 1 289.03 5 1 1770.7 6 1 292.84 5 1 1760.93 6 1 297.27 5 1 1750.06 6 1 303.15 5 1 1734.49 6 1 307.51 5 1 1722.71 6 1 312.58 5 1 1709.52 6 423552 1 Principal objective of the work HR HR 5/8/2007 1 Mass density, kg/m3 Pycnometric method Liquid Direct value, X Liquid Gas 1 Temperature, K 1 288.63 5 1 1926.65 6 1 292.57 5 1 1917 6 1 298.78 5 1 1906.56 6 1 302.71 5 1 1892.19 6 1 307.01 5 1 1881.37 6 1 311.72 5 1 1869.53 6 80793175 1 Principal objective of the work RDC TRC 7/5/2007 1 Mass density, kg/m3 Pycnometric method Liquid Direct value, X Liquid Gas 1 Temperature, K 1 288.93 5 1 1566.26 6 1 292.66 5 1 1558.07 6 1 298.73 5 1 1545.55 6 1 302.86 5 1 1536.04 6 1 307.25 5 1 1527.24 6 1 312.48 5 1 1515.63 6 80793175 1 Principal objective of the work RDC TRC 7/5/2007 1 Vapor or sublimation pressure, kPa Closed cell (Static) method Liquid Direct value, X Liquid Gas 1 Temperature, K 1 Author 1 298.3 5 1 4.9783 5 1 298.32 5 1 4.9709 5 1 303.21 5 1 5.8818 5 1 307.81 5 1 6.9263 5 1 312.81 5 1 8.1306 5 124389 1 307346 1 Principal objective of the work HR HR 5/8/2007 1 Ostwald coefficient gas volume change or dissolution Liquid Direct value, X 307346 Liquid Gas Partial pressure, kPa 124389 Liquid 100 3 1 Temperature, K 1 289.79 5 1 2.17 3 1 293.53 5 1 2.11 3 1 297.18 5 1 2.02 3 1 303.12 5 1 1.93 3 1 307.33 5 1 1.86 3 1 311 5 1 1.76 3 124389 1 423552 1 Principal objective of the work HR HR 5/8/2007 1 Ostwald coefficient gas volume change or dissolution Liquid Direct value, X 423552 Liquid Gas Partial pressure, kPa 124389 Liquid 100 3 1 Temperature, K 1 289.15 5 1 2.41 3 1 293.45 5 1 2.36 3 1 298.81 5 1 2.23 3 1 302.93 5 1 2.08 3 1 307.1 5 1 2.02 3 1 311.12 5 1 1.93 3 124389 1 306945 1 Principal objective of the work HR HR 5/8/2007 1 Ostwald coefficient gas volume change or dissolution Liquid Direct value, X 306945 Liquid Gas Partial pressure, kPa 124389 Liquid 100 3 1 Temperature, K 1 288.59 5 1 1.93 3 1 292.28 5 1 1.92 3 1 296.62 5 1 1.77 3 1 302.73 5 1 1.61 3 1 306.91 5 1 1.6 3 1 311.41 5 1 1.57 3 124389 1 355022 1 Principal objective of the work HR HR 5/8/2007 1 Ostwald coefficient gas volume change or dissolution Liquid Direct value, X 355022 Liquid Gas Partial pressure, kPa 124389 Liquid 100 3 1 Temperature, K 1 289.15 5 1 2.33 3 1 292.42 5 1 2.19 3 1 296.69 5 1 2.11 3 1 302.94 5 1 1.97 3 1 306.66 5 1 1.83 3 1 311.17 5 1 1.63 3 124389 1 335273 1 Principal objective of the work HR HR 5/8/2007 1 Ostwald coefficient gas volume change or dissolution Liquid Direct value, X 335273 Liquid Gas Partial pressure, kPa 124389 Liquid 100 3 1 Temperature, K 1 288.83 5 1 2.2 3 1 292.08 5 1 2.12 3 1 296.43 5 1 1.99 3 1 302.68 5 1 1.9 3 1 306.72 5 1 1.72 3 1 306.58 5 1 1.74 3 1 310.89 5 1 1.71 3 124389 1 306912 1 Principal objective of the work HR HR 5/8/2007 1 Ostwald coefficient gas volume change or dissolution Liquid Direct value, X 306912 Liquid Gas Partial pressure, kPa 124389 Liquid 100 3 1 Temperature, K 1 292.22 5 1 1.63 3 1 296.73 5 1 1.53 3 1 302.44 5 1 1.4 3 1 311.14 5 1 1.19 3 307346 1 630080 1 Principal objective of the work HR HR 5/8/2007 1 Ostwald coefficient gas volume change or dissolution Liquid Direct value, X 307346 Liquid Gas Partial pressure, kPa 630080 Liquid 100 3 1 Temperature, K 1 289.86 5 1 .37 3 1 292.28 5 1 .375 3 1 302.54 5 1 .378 3 1 306.78 5 1 .369 3 1 311.04 5 1 .368 3 423552 1 630080 1 Principal objective of the work HR HR 5/8/2007 1 Ostwald coefficient gas volume change or dissolution Liquid Direct value, X 423552 Liquid Gas Partial pressure, kPa 630080 Liquid 100 3 1 Temperature, K 1 288.89 5 1 .338 3 1 292.4 5 1 .345 3 1 302.52 5 1 .34 3 1 307.23 5 1 .338 3 1 311.07 5 1 .345 3 124389 1 80793175 1 Principal objective of the work RDC TRC 7/5/2007 1 Ostwald coefficient x Liquid Direct value, X 80793175 Liquid Gas Partial pressure, kPa 124389 Liquid 100 3 1 Temperature, K 1 289.3 5 1 2.87 3 1 293.3 5 1 2.8 3 1 296.82 5 1 2.74 3 1 302.68 5 1 2.58 3 1 305.12 5 1 2.49 3 1 311.36 5 1 2.27 3 630080 1 80793175 1 Principal objective of the work RDC TRC 7/5/2007 1 Ostwald coefficient x Liquid Direct value, X 80793175 Liquid Gas Partial pressure, kPa 630080 Liquid 100 3 1 Temperature, K 1 289.04 5 1 .393 3 1 295.56 5 1 .392 3 1 304.24 5 1 .389 3 1 306.88 5 1 .392 3 1 311.13 5 1 .391 3