2 0 2009 per gin 0 journal Original Perez-Gregorio, V. Giner, D. M. B. Royo, C. L. F. M. J. Chem. Thermodyn. 2009 2009-04-07 Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures 1-Chloroalkane n-Hexane Surface tension (Vapour + liquid) equilibrium 10.1016/j.jct.2008.10.016 41 553-559 1 hexane C6H14 1 Commercial source 1 99 2 Stated by supplier 2 None used 2 1-chlorobutane C4H9Cl 1 Commercial source 1 99 2 Stated by supplier 2 None used 3 1-chloropentane C5H11Cl 1 Commercial source 1 99 2 Stated by supplier 2 None used 1 1 Principal objective of the work WZ TRC 2/10/2009 1 Surface tension liquid-gas, N/m Drop volume Liquid Direct value, X 1 Author Liquid Gas 1 Temperature, K 1 Author 1 283.15 5 1 .01963 4 1 .00009815 1 288.15 5 1 .01904 4 1 .0000952 1 293.15 5 1 .01852 4 1 .0000926 1 298.15 5 1 .01806 4 1 .0000903 1 303.15 5 1 .01753 4 1 .00008765 1 308.15 5 1 .01674 4 1 .0000837 1 313.15 5 1 .01647 4 1 .00008235 2 1 Principal objective of the work WZ TRC 2/10/2009 1 Surface tension liquid-gas, N/m Drop volume Liquid Direct value, X 1 Author Liquid Gas 1 Temperature, K 1 Author 1 283.15 5 1 .02473 4 1 .00012365 1 288.15 5 1 .02424 4 1 .0001212 1 293.15 5 1 .02364 4 1 .0001182 1 298.15 5 1 .02329 4 1 .00011645 1 303.15 5 1 .02262 4 1 .0001131 1 308.15 5 1 .02203 4 1 .00011015 1 313.15 5 1 .02153 4 1 .00010765 3 1 Principal objective of the work WZ TRC 2/10/2009 1 Surface tension liquid-gas, N/m Drop volume Liquid Direct value, X 1 Author Liquid Gas 1 Temperature, K 1 Author 1 283.15 5 1 .02602 4 1 .0001301 1 288.15 5 1 .02558 4 1 .0001279 1 293.15 5 1 .02502 4 1 .0001251 1 298.15 5 1 .02446 4 1 .0001223 1 303.15 5 1 .02402 4 1 .0001201 1 308.15 5 1 .02351 4 1 .00011755 1 313.15 5 1 .02302 4 1 .0001151 2 1 1 1 Principal objective of the work WZ TRC 2/10/2009 1 Surface tension liquid-gas, N/m Drop volume Liquid Direct value, X 1 Author Liquid Gas 1 Temperature, K 1 Author 2 Mole fraction 1 Liquid 1 Author 1 283.15 5 2 .0493 3 1 .02417 4 1 .00012085 1 283.15 5 2 .1016 4 1 .0237 4 1 .0001185 1 283.15 5 2 .2048 4 1 .02296 4 1 .0001148 1 283.15 5 2 .3038 4 1 .02232 4 1 .0001116 1 283.15 5 2 .3967 4 1 .02182 4 1 .0001091 1 283.15 5 2 .5015 4 1 .02129 4 1 .00010645 1 283.15 5 2 .6086 4 1 .02085 4 1 .00010425 1 283.15 5 2 .7097 4 1 .02048 4 1 .0001024 1 283.15 5 2 .804 4 1 .02019 4 1 .00010095 1 283.15 5 2 .9021 4 1 .01991 4 1 .00009955 1 283.15 5 2 .9391 4 1 .01981 4 1 .00009905 1 288.15 5 2 .0493 3 1 .02368 4 1 .0001184 1 288.15 5 2 .1016 4 1 .02321 4 1 .00011605 1 288.15 5 2 .2048 4 1 .02246 4 1 .0001123 1 288.15 5 2 .3038 4 1 .02183 4 1 .00010915 1 288.15 5 2 .3967 4 1 .02132 4 1 .0001066 1 288.15 5 2 .5015 4 1 .02078 4 1 .0001039 1 288.15 5 2 .6086 4 1 .02031 4 1 .00010155 1 288.15 5 2 .7097 4 1 .01993 4 1 .00009965 1 288.15 5 2 .804 4 1 .01963 4 1 .00009815 1 288.15 5 2 .9021 4 1 .01935 4 1 .00009675 1 288.15 5 2 .9391 4 1 .01924 4 1 .0000962 1 293.15 5 2 .0493 3 1 .02311 4 1 .00011555 1 293.15 5 2 .1016 4 1 .02263 4 1 .00011315 1 293.15 5 2 .2048 4 1 .02188 4 1 .0001094 1 293.15 5 2 .3038 4 1 .02128 4 1 .0001064 1 293.15 5 2 .3967 4 1 .02079 4 1 .00010395 1 293.15 5 2 .5015 4 1 .02025 4 1 .00010125 1 293.15 5 2 .6086 4 1 .01977 4 1 .00009885 1 293.15 5 2 .7097 4 1 .0194 4 1 .000097 1 293.15 5 2 .804 4 1 .0191 4 1 .0000955 1 293.15 5 2 .9021 4 1 .01884 4 1 .0000942 1 293.15 5 2 .9391 4 1 .01873 4 1 .00009365 1 298.15 5 2 .0493 3 1 .02274 4 1 .0001137 1 298.15 5 2 .1016 4 1 .02227 4 1 .00011135 1 298.15 5 2 .2048 4 1 .02152 4 1 .0001076 1 298.15 5 2 .3038 4 1 .02093 4 1 .00010465 1 298.15 5 2 .3967 4 1 .02043 4 1 .00010215 1 298.15 5 2 .5015 4 1 .01989 4 1 .00009945 1 298.15 5 2 .6086 4 1 .01939 4 1 .00009695 1 298.15 5 2 .7097 4 1 .019 4 1 .000095 1 298.15 5 2 .804 4 1 .01871 4 1 .00009355 1 298.15 5 2 .9021 4 1 .01843 4 1 .00009215 1 298.15 5 2 .9391 4 1 .01831 4 1 .00009155 1 303.15 5 2 .0493 3 1 .02208 4 1 .0001104 1 303.15 5 2 .1016 4 1 .02162 4 1 .0001081 1 303.15 5 2 .2048 4 1 .02089 4 1 .00010445 1 303.15 5 2 .3038 4 1 .02032 4 1 .0001016 1 303.15 5 2 .3967 4 1 .01983 4 1 .00009915 1 303.15 5 2 .5015 4 1 .01931 4 1 .00009655 1 303.15 5 2 .6086 4 1 .01882 4 1 .0000941 1 303.15 5 2 .7097 4 1 .01846 4 1 .0000923 1 303.15 5 2 .804 4 1 .01818 4 1 .0000909 1 303.15 5 2 .9021 4 1 .01791 4 1 .00008955 1 303.15 5 2 .9391 4 1 .01779 4 1 .00008895 1 308.15 5 2 .0493 3 1 .0215 4 1 .0001075 1 308.15 5 2 .1016 4 1 .02103 4 1 .00010515 1 308.15 5 2 .2048 4 1 .02028 4 1 .0001014 1 308.15 5 2 .3038 4 1 .01969 4 1 .00009845 1 308.15 5 2 .3967 4 1 .01918 4 1 .0000959 1 308.15 5 2 .5015 4 1 .01864 4 1 .0000932 1 308.15 5 2 .6086 4 1 .01814 4 1 .0000907 1 308.15 5 2 .7097 4 1 .01777 4 1 .00008885 1 308.15 5 2 .804 4 1 .01746 4 1 .0000873 1 308.15 5 2 .9021 4 1 .01716 4 1 .0000858 1 308.15 5 2 .9391 4 1 .01702 4 1 .0000851 1 313.15 5 2 .0493 3 1 .02104 4 1 .0001052 1 313.15 5 2 .1016 4 1 .02059 4 1 .00010295 1 313.15 5 2 .2048 4 1 .01984 4 1 .0000992 1 313.15 5 2 .3038 4 1 .01928 4 1 .0000964 1 313.15 5 2 .3967 4 1 .01879 4 1 .00009395 1 313.15 5 2 .5015 4 1 .01827 4 1 .00009135 1 313.15 5 2 .6086 4 1 .01781 4 1 .00008905 1 313.15 5 2 .7097 4 1 .01747 4 1 .00008735 1 313.15 5 2 .804 4 1 .01718 4 1 .0000859 1 313.15 5 2 .9021 4 1 .01689 4 1 .00008445 1 313.15 5 2 .9391 4 1 .01675 4 1 .00008375 2 1 1 1 Principal objective of the work WZ TRC 2/10/2009 1 Vapor or sublimation pressure, kPa Ebulliometric method (Recirculating still) Liquid Direct value, X 1 Author Liquid Gas 1 Mole fraction 1 Gas 1 Author 2 Temperature, K 1 Author 1 .1449 4 2 288.15 5 1 9.21 4 1 .000921 1 .2894 4 2 288.15 5 1 10.12 5 1 .001012 1 .3509 4 2 288.15 5 1 10.45 5 1 .001045 1 .4148 4 2 288.15 5 1 10.9 5 1 .00109 1 .4642 4 2 288.15 5 1 11.2 5 1 .00112 1 .5464 4 2 288.15 5 1 11.7 5 1 .00117 1 .649 4 2 288.15 5 1 12.2 5 1 .00122 1 .723 4 2 288.15 5 1 12.52 5 1 .001252 1 .7588 4 2 288.15 5 1 12.62 5 1 .001262 1 .8 4 2 288.15 5 1 12.73 5 1 .001273 1 .8526 4 2 288.15 5 1 12.8 5 1 .00128 1 .9126 4 2 288.15 5 1 12.9 5 1 .00129 1 .9505 4 2 288.15 5 1 12.91 5 1 .001291 1 .1247 4 2 298.15 5 1 14.45 5 1 .001445 1 .1675 4 2 298.15 5 1 15 5 1 .0015 1 .3055 4 2 298.15 5 1 16.165 5 1 .0016165 1 .3848 4 2 298.15 5 1 16.965 5 1 .0016965 1 .4333 4 2 298.15 5 1 17.47 5 1 .001747 1 .5405 4 2 298.15 5 1 18.44 5 1 .001844 1 .5946 4 2 298.15 5 1 18.875 5 1 .0018875 1 .6581 4 2 298.15 5 1 19.32 5 1 .001932 1 .7024 4 2 298.15 5 1 19.605 5 1 .0019605 1 .7387 4 2 298.15 5 1 19.78 5 1 .001978 1 .8128 4 2 298.15 5 1 20.12 5 1 .002012 1 .8798 4 2 298.15 5 1 20.27 5 1 .002027 1 .9345 4 2 298.15 5 1 20.315 5 1 .0020315 1 .1447 4 2 308.15 5 1 22.93 5 1 .002293 1 .2319 4 2 308.15 5 1 24 5 1 .0024 1 .3069 4 2 308.15 5 1 25.09 5 1 .002509 1 .3853 4 2 308.15 5 1 26.14 5 1 .002614 1 .474 4 2 308.15 5 1 27.36 5 1 .002736 1 .5308 4 2 308.15 5 1 28.05 5 1 .002805 1 .5805 4 2 308.15 5 1 28.67 5 1 .002867 1 .6488 4 2 308.15 5 1 29.38 5 1 .002938 1 .7067 4 2 308.15 5 1 29.96 5 1 .002996 1 .7067 4 2 308.15 5 1 30.13 5 1 .003013 1 .8078 4 2 308.15 5 1 30.56 5 1 .003056 1 .9135 4 2 308.15 5 1 30.855 5 1 .0030855 1 .9508 4 2 308.15 5 1 30.8 5 1 .00308 2 1 1 1 Principal objective of the work WZ TRC 2/10/2009 1 Mole fraction Density calibration data 1 Liquid Direct value, X 1 Author Liquid Gas 1 Mole fraction 1 Gas 1 Author 2 Temperature, K 1 Author 1 .1449 4 2 288.15 5 1 .0704 3 1 .0000001408 1 .2894 4 2 288.15 5 1 .1602 4 1 .0000003204 1 .3509 4 2 288.15 5 1 .2102 4 1 .0000004204 1 .4148 4 2 288.15 5 1 .2795 4 1 .000000559 1 .4642 4 2 288.15 5 1 .3264 4 1 .0000006528 1 .5464 4 2 288.15 5 1 .4303 4 1 .0000008606 1 .649 4 2 288.15 5 1 .5617 4 1 .0000011234 1 .723 4 2 288.15 5 1 .6599 4 1 .0000013198 1 .7588 4 2 288.15 5 1 .728 4 1 .000001456 1 .8 4 2 288.15 5 1 .7648 4 1 .0000015296 1 .8526 4 2 288.15 5 1 .84 4 1 .00000168 1 .9126 4 2 288.15 5 1 .9184 4 1 .0000018368 1 .9505 4 2 288.15 5 1 .9516 4 1 .0000019032 1 .1247 4 2 298.15 5 1 .0619 3 1 .0000001238 1 .1675 4 2 298.15 5 1 .0859 3 1 .0000001718 1 .3055 4 2 298.15 5 1 .1867 4 1 .0000003734 1 .3848 4 2 298.15 5 1 .2508 4 1 .0000005016 1 .4333 4 2 298.15 5 1 .3061 4 1 .0000006122 1 .5405 4 2 298.15 5 1 .4251 4 1 .0000008502 1 .5946 4 2 298.15 5 1 .4916 4 1 .0000009832 1 .6581 4 2 298.15 5 1 .5768 4 1 .0000011536 1 .7024 4 2 298.15 5 1 .64 4 1 .00000128 1 .7387 4 2 298.15 5 1 .7003 4 1 .0000014006 1 .8128 4 2 298.15 5 1 .7901 4 1 .0000015802 1 .8798 4 2 298.15 5 1 .8767 4 1 .0000017534 1 .9345 4 2 298.15 5 1 .9334 4 1 .0000018668 1 .1447 4 2 308.15 5 1 .0758 3 1 .0000001516 1 .2319 4 2 308.15 5 1 .1321 4 1 .0000002642 1 .3069 4 2 308.15 5 1 .1898 4 1 .0000003796 1 .3853 4 2 308.15 5 1 .2636 4 1 .0000005272 1 .474 4 2 308.15 5 1 .3549 4 1 .0000007098 1 .5308 4 2 308.15 5 1 .4193 4 1 .0000008386 1 .5805 4 2 308.15 5 1 .4804 4 1 .0000009608 1 .6488 4 2 308.15 5 1 .5729 4 1 .0000011458 1 .7067 4 2 308.15 5 1 .6531 4 1 .0000013062 1 .7067 4 2 308.15 5 1 .697 4 1 .000001394 1 .8078 4 2 308.15 5 1 .784 4 1 .000001568 1 .9135 4 2 308.15 5 1 .9112 4 1 .0000018224 1 .9508 4 2 308.15 5 1 .9513 4 1 .0000019026 1 1 3 1 Principal objective of the work WZ TRC 2/10/2009 1 Surface tension liquid-gas, N/m Drop volume Liquid Direct value, X 1 Author Liquid Gas 1 Temperature, K 1 Author 2 Mole fraction 1 Liquid 1 Author 1 283.15 5 2 .0482 3 1 .02544 4 1 .0001272 1 283.15 5 2 .1185 4 1 .0247 4 1 .0001235 1 283.15 5 2 .1991 4 1 .024 4 1 .00012 1 283.15 5 2 .308 4 1 .0232 4 1 .000116 1 283.15 5 2 .3925 4 1 .02262 4 1 .0001131 1 283.15 5 2 .5087 4 1 .02191 4 1 .00010955 1 283.15 5 2 .5953 4 1 .02141 4 1 .00010705 1 283.15 5 2 .7076 4 1 .02085 4 1 .00010425 1 283.15 5 2 .7889 4 1 .02047 4 1 .00010235 1 283.15 5 2 .9069 4 1 .01997 4 1 .00009985 1 283.15 5 2 .9474 4 1 .01981 4 1 .00009905 1 288.15 5 2 .0482 3 1 .02502 4 1 .0001251 1 288.15 5 2 .1185 4 1 .0243 4 1 .0001215 1 288.15 5 2 .1991 4 1 .02359 4 1 .00011795 1 288.15 5 2 .308 4 1 .02276 4 1 .0001138 1 288.15 5 2 .3925 4 1 .02217 4 1 .00011085 1 288.15 5 2 .5087 4 1 .02144 4 1 .0001072 1 288.15 5 2 .5953 4 1 .02094 4 1 .0001047 1 288.15 5 2 .7076 4 1 .02037 4 1 .00010185 1 288.15 5 2 .7889 4 1 .01998 4 1 .0000999 1 288.15 5 2 .9069 4 1 .01944 4 1 .0000972 1 288.15 5 2 .9474 4 1 .01924 4 1 .0000962 1 293.15 5 2 .0482 3 1 .02453 4 1 .00012265 1 293.15 5 2 .1185 4 1 .02383 4 1 .00011915 1 293.15 5 2 .1991 4 1 .02309 4 1 .00011545 1 293.15 5 2 .308 4 1 .02225 4 1 .00011125 1 293.15 5 2 .3925 4 1 .02167 4 1 .00010835 1 293.15 5 2 .5087 4 1 .02094 4 1 .0001047 1 293.15 5 2 .5953 4 1 .02047 4 1 .00010235 1 293.15 5 2 .7076 4 1 .0199 4 1 .0000995 1 293.15 5 2 .7889 4 1 .0195 4 1 .0000975 1 293.15 5 2 .9069 4 1 .01894 4 1 .0000947 1 293.15 5 2 .9474 4 1 .01874 4 1 .0000937 1 298.15 5 2 .0482 3 1 .02402 4 1 .0001201 1 298.15 5 2 .1185 4 1 .02335 4 1 .00011675 1 298.15 5 2 .1991 4 1 .02264 4 1 .0001132 1 298.15 5 2 .308 4 1 .02178 4 1 .0001089 1 298.15 5 2 .3925 4 1 .0212 4 1 .000106 1 298.15 5 2 .5087 4 1 .02047 4 1 .00010235 1 298.15 5 2 .5953 4 1 .02002 4 1 .0001001 1 298.15 5 2 .7076 4 1 .01945 4 1 .00009725 1 298.15 5 2 .7889 4 1 .01904 4 1 .0000952 1 298.15 5 2 .9069 4 1 .0185 4 1 .0000925 1 298.15 5 2 .9474 4 1 .01829 4 1 .00009145 1 303.15 5 2 .0482 3 1 .02359 4 1 .00011795 1 303.15 5 2 .1185 4 1 .02295 4 1 .00011475 1 303.15 5 2 .1991 4 1 .02224 4 1 .0001112 1 303.15 5 2 .308 4 1 .02137 4 1 .00010685 1 303.15 5 2 .3925 4 1 .02075 4 1 .00010375 1 303.15 5 2 .5087 4 1 .02003 4 1 .00010015 1 303.15 5 2 .5953 4 1 .01956 4 1 .0000978 1 303.15 5 2 .7076 4 1 .01898 4 1 .0000949 1 303.15 5 2 .7889 4 1 .01856 4 1 .0000928 1 303.15 5 2 .9069 4 1 .01799 4 1 .00008995 1 303.15 5 2 .9474 4 1 .01779 4 1 .00008895 1 308.15 5 2 .0482 3 1 .02311 4 1 .00011555 1 308.15 5 2 .1185 4 1 .02245 4 1 .00011225 1 308.15 5 2 .1991 4 1 .02171 4 1 .00010855 1 308.15 5 2 .308 4 1 .0208 4 1 .000104 1 308.15 5 2 .3925 4 1 .02016 4 1 .0001008 1 308.15 5 2 .5087 4 1 .0194 4 1 .000097 1 308.15 5 2 .5953 4 1 .01891 4 1 .00009455 1 308.15 5 2 .7076 4 1 .0183 4 1 .0000915 1 308.15 5 2 .7889 4 1 .01788 4 1 .0000894 1 308.15 5 2 .9069 4 1 .01725 4 1 .00008625 1 308.15 5 2 .9474 4 1 .01705 4 1 .00008525 1 313.15 5 2 .0482 3 1 .02264 4 1 .0001132 1 313.15 5 2 .1185 4 1 .02202 4 1 .0001101 1 313.15 5 2 .1991 4 1 .0213 4 1 .0001065 1 313.15 5 2 .308 4 1 .02041 4 1 .00010205 1 313.15 5 2 .3925 4 1 .0198 4 1 .000099 1 313.15 5 2 .5087 4 1 .01905 4 1 .00009525 1 313.15 5 2 .5953 4 1 .01856 4 1 .0000928 1 313.15 5 2 .7076 4 1 .018 4 1 .00009 1 313.15 5 2 .7889 4 1 .01758 4 1 .0000879 1 313.15 5 2 .9069 4 1 .01699 4 1 .00008495 1 313.15 5 2 .9474 4 1 .01677 4 1 .00008385 1 1 3 1 Principal objective of the work WZ TRC 2/10/2009 1 Vapor or sublimation pressure, kPa Ebulliometric method (Recirculating still) Liquid Direct value, X 1 Author Liquid Gas 1 Mole fraction 1 Gas 1 Author 2 Temperature, K 1 Author 1 .4075 4 2 288.15 5 1 3.68 4 1 .000368 1 .5479 4 2 288.15 5 1 4.385 4 1 .0004385 1 .6274 4 2 288.15 5 1 5.07 4 1 .000507 1 .7251 4 2 288.15 5 1 6.215 4 1 .0006215 1 .8005 4 2 288.15 5 1 7.5 4 1 .00075 1 .8488 4 2 288.15 5 1 8.645 4 1 .0008645 1 .8727 4 2 288.15 5 1 9.3 4 1 .00093 1 .9044 4 2 288.15 5 1 10.105 5 1 .0010105 1 .9294 4 2 288.15 5 1 11 5 1 .0011 1 .9417 4 2 288.15 5 1 11.285 5 1 .0011285 1 .3178 4 2 288.15 5 1 5.625 4 1 .0005625 1 .3178 4 2 298.15 5 1 5.625 4 1 .0005625 1 .4289 4 2 298.15 5 1 6.57 4 1 .000657 1 .5969 4 2 298.15 5 1 8.325 4 1 .0008325 1 .7387 4 2 298.15 5 1 10.93 5 1 .001093 1 .7966 4 2 298.15 5 1 12.755 5 1 .0012755 1 .8467 4 2 298.15 5 1 14.34 5 1 .001434 1 .8741 4 2 298.15 5 1 15.055 5 1 .0015055 1 .8983 4 2 298.15 5 1 16.255 5 1 .0016255 1 .9287 4 2 298.15 5 1 17.27 5 1 .001727 1 .9445 4 2 298.15 5 1 18.095 5 1 .0018095 1 .9683 4 2 298.15 5 1 18.91 5 1 .001891 1 .9799 4 2 298.15 5 1 19.42 5 1 .001942 1 .2359 4 2 308.15 5 1 8.49 4 1 .000849 1 .3706 4 2 308.15 5 1 9.9 4 1 .00099 1 .448 4 2 308.15 5 1 10.9 5 1 .00109 1 .5497 4 2 308.15 5 1 12.47 5 1 .001247 1 .652 4 2 308.15 5 1 15 5 1 .0015 1 .6902 4 2 308.15 5 1 16.155 5 1 .0016155 1 .794 4 2 308.15 5 1 20.005 5 1 .0020005 1 .8407 4 2 308.15 5 1 22.045 5 1 .0022045 1 .8812 4 2 308.15 5 1 23.9 5 1 .00239 1 .92 4 2 308.15 5 1 26.12 5 1 .002612 1 .9423 4 2 308.15 5 1 27.315 5 1 .0027315 1 .9728 4 2 308.15 5 1 29.105 5 1 .0029105 1 1 3 1 Principal objective of the work WZ TRC 2/10/2009 1 Mole fraction Density calibration data 1 Liquid Direct value, X 1 Author Liquid Gas 1 Mole fraction 1 Gas 1 Author 2 Temperature, K 1 Author 1 .4075 4 2 288.15 5 1 .0769 3 1 .0000001538 1 .5479 4 2 288.15 5 1 .1328 4 1 .0000002656 1 .6274 4 2 288.15 5 1 .1792 4 1 .0000003584 1 .7251 4 2 288.15 5 1 .2697 4 1 .0000005394 1 .8005 4 2 288.15 5 1 .3753 4 1 .0000007506 1 .8488 4 2 288.15 5 1 .4962 4 1 .0000009924 1 .8727 4 2 288.15 5 1 .5668 4 1 .0000011336 1 .9044 4 2 288.15 5 1 .6557 4 1 .0000013114 1 .9294 4 2 288.15 5 1 .7586 4 1 .0000015172 1 .9417 4 2 288.15 5 1 .7999 4 1 .0000015998 1 .3178 4 2 288.15 5 1 .0643 3 1 .0000001286 1 .3178 4 2 298.15 5 1 .0643 3 1 .0000001286 1 .4289 4 2 298.15 5 1 .1033 4 1 .0000002066 1 .5969 4 2 298.15 5 1 .1898 4 1 .0000003796 1 .7387 4 2 298.15 5 1 .3239 4 1 .0000006478 1 .7966 4 2 298.15 5 1 .4282 4 1 .0000008564 1 .8467 4 2 298.15 5 1 .542 4 1 .000001084 1 .8741 4 2 298.15 5 1 .5964 4 1 .0000011928 1 .8983 4 2 298.15 5 1 .679 4 1 .000001358 1 .9287 4 2 298.15 5 1 .7621 4 1 .0000015242 1 .9445 4 2 298.15 5 1 .8296 4 1 .0000016592 1 .9683 4 2 298.15 5 1 .8998 4 1 .0000017996 1 .9799 4 2 298.15 5 1 .9395 4 1 .000001879 1 .2359 4 2 308.15 5 1 .0471 3 1 .0000000942 1 .3706 4 2 308.15 5 1 .0863 3 1 .0000001726 1 .448 4 2 308.15 5 1 .1188 4 1 .0000002376 1 .5497 4 2 308.15 5 1 .1711 4 1 .0000003422 1 .652 4 2 308.15 5 1 .2514 4 1 .0000005028 1 .6902 4 2 308.15 5 1 .3004 4 1 .0000006008 1 .794 4 2 308.15 5 1 .4506 4 1 .0000009012 1 .8407 4 2 308.15 5 1 .5483 4 1 .0000010966 1 .8812 4 2 308.15 5 1 .644 4 1 .000001288 1 .92 4 2 308.15 5 1 .753 4 1 .000001506 1 .9423 4 2 308.15 5 1 .8221 4 1 .0000016442 1 .9728 4 2 308.15 5 1 .9195 4 1 .000001839