2 0 2009 cou soo 0 journal Original Courtial, X.[Xavier] Soo, C.-B.[Chien-Bin] Coquelet, C.[Christophe] Paricaud, P.[Patrice] Ramjugernath, D.[Deresh] Richon, D.[Dominique] Fluid Phase Equilib. 2009 2009-04-01 Vapor liquid equilibrium in the n-butane +methanol system, measurement and modeling from 323.2 to 443.2K Experimental VLE measurement n-Butane Methanol Critical temperature Thermodynamic model 10.1016/j.fluid.2008.12.001 277 152-161 1 butane C4H10 1 Commercial source 1 99.95 4 Stated by supplier 2 methanol CH4O 1 Commercial source 1 99.93 4 Stated by supplier 2 1 1 1 Principal objective of the work PW TRC 3/5/2009 1 Vapor or sublimation pressure, kPa Closed cell (Static) method Liquid Direct value, X 1 Author Liquid Gas 1 Mole fraction 1 Liquid 1 Author 2 Temperature, K 1 Author 1 .0699 3 2 323.22 5 1 336.6 4 1 4.2 1 .104 4 2 323.22 5 1 399.7 4 1 4.2 1 .1955 4 2 323.22 5 1 483.8 4 1 4.2 1 .316 4 2 323.22 5 1 510.6 4 1 4.2 1 .434 4 2 323.22 5 1 521.7 4 1 4.2 1 .6224 4 2 323.22 5 1 522.9 4 1 4.2 1 .6874 4 2 323.22 5 1 525.3 4 1 4.2 1 .831 4 2 323.22 5 1 526.6 4 1 4.2 1 .9178 4 2 323.22 5 1 528.5 4 1 4.2 1 .9632 4 2 323.22 5 1 525.1 4 1 4.2 1 .9733 4 2 323.22 5 1 522.6 4 1 4.2 1 .0178 3 2 373.19 5 1 571.5 4 1 4.2 1 .0579 3 2 373.19 5 1 955.6 4 1 4.2 1 .1074 4 2 373.19 5 1 1242.8 5 1 4.2 1 .1683 4 2 373.19 5 1 1427.6 5 1 4.2 1 .2585 4 2 373.19 5 1 1553.4 5 1 4.2 1 .3777 4 2 373.19 5 1 1638.3 5 1 4.2 1 .5706 4 2 373.19 5 1 1687.4 5 1 4.2 1 .7229 4 2 373.19 5 1 1711.8 5 1 4.2 1 .78 4 2 373.19 5 1 1719.8 5 1 4.2 1 .8979 4 2 373.19 5 1 1720.2 5 1 4.2 1 .9256 4 2 373.19 5 1 1709.4 5 1 4.2 1 .9879 4 2 373.19 5 1 1583.1 5 1 4.2 1 .9884 4 2 373.19 5 1 1582.5 5 1 4.2 1 .0192 3 2 403.13 5 1 1175 5 1 4.2 1 .0577 3 2 403.13 5 1 1671 5 1 4.2 1 .0959 3 2 403.13 5 1 2149.8 5 1 4.2 1 .1625 4 2 403.13 5 1 2500.7 5 1 4.2 1 .3141 4 2 403.13 5 1 2830.4 5 1 4.2 1 .4959 4 2 403.13 5 1 2957.7 5 1 4.2 1 .6971 4 2 403.13 5 1 3057.2 5 1 4.2 1 .8183 4 2 403.13 5 1 3091.1 5 1 4.2 1 .8986 4 2 403.13 5 1 3037 5 1 4.2 1 .9429 4 2 403.13 5 1 2928.6 5 1 4.2 1 .9918 4 2 403.13 5 1 2688.5 5 1 4.2 1 .0191 3 2 423.09 5 1 1963.7 5 1 4.2 1 .0488 3 2 423.09 5 1 2472.1 5 1 4.2 1 .1095 4 2 423.09 5 1 3036.6 5 1 4.2 1 .1915 4 2 423.09 5 1 3575.1 5 1 4.2 1 .3062 4 2 423.09 5 1 3963.6 5 1 4.2 1 .5195 4 2 423.09 5 1 4210.1 5 1 4.2 1 .7128 4 2 423.09 5 1 4374.2 5 1 4.2 1 .0094 2 2 433.16 5 1 2082.2 5 1 4.2 1 .0146 3 2 433.16 5 1 2197.2 5 1 4.2 1 .0259 3 2 433.16 5 1 2569.6 5 1 4.2 1 .0448 3 2 433.16 5 1 3011.2 5 1 4.2 1 .0883 3 2 433.16 5 1 3503.3 5 1 4.2 1 .0924 3 2 433.16 5 1 3543.4 5 1 4.2 1 .1559 4 2 433.16 5 1 4029.4 5 1 4.2 1 .1582 4 2 433.16 5 1 4054.4 5 1 4.2 1 .2425 4 2 433.16 5 1 4415 5 1 4.2 1 .2794 4 2 433.16 5 1 4594.2 5 1 4.2 1 .4244 4 2 433.16 5 1 4844.7 5 1 4.2 1 .0113 3 2 443.19 5 1 2453.9 5 1 4.2 1 .0377 3 2 443.19 5 1 3056.7 5 1 4.2 1 .064 3 2 443.19 5 1 3493.8 5 1 4.2 1 .0917 3 2 443.19 5 1 3908.6 5 1 4.2 1 .1515 4 2 443.19 5 1 4553.4 5 1 4.2 1 .2299 4 2 443.19 5 1 5008.2 5 1 4.2 1 .3688 4 2 443.19 5 1 5434.5 5 1 4.2 2 1 1 1 Principal objective of the work PW TRC 3/5/2009 1 Mole fraction Chromatography 2 Gas Direct value, X 1 Author Gas Liquid 1 Mole fraction 1 Liquid 1 Author 2 Temperature, K 1 Author 1 .0699 3 2 323.22 5 1 .8409 4 1 .0042 1 .104 4 2 323.22 5 1 .8713 4 1 .0042 1 .1955 4 2 323.22 5 1 .8985 4 1 .0042 1 .316 4 2 323.22 5 1 .9059 4 1 .0042 1 .434 4 2 323.22 5 1 .9097 4 1 .0042 1 .6224 4 2 323.22 5 1 .9122 4 1 .0042 1 .6874 4 2 323.22 5 1 .9127 4 1 .0042 1 .831 4 2 323.22 5 1 .9159 4 1 .0042 1 .9178 4 2 323.22 5 1 .9224 4 1 .0042 1 .9632 4 2 323.22 5 1 .9332 4 1 .0042 1 .9733 4 2 323.22 5 1 .9385 4 1 .0042 1 .0178 3 2 373.19 5 1 .3675 4 1 .0042 1 .0579 3 2 373.19 5 1 .6318 4 1 .0042 1 .1074 4 2 373.19 5 1 .735 4 1 .0042 1 .1683 4 2 373.19 5 1 .7733 4 1 .0042 1 .2585 4 2 373.19 5 1 .7971 4 1 .0042 1 .3777 4 2 373.19 5 1 .8127 4 1 .0042 1 .5706 4 2 373.19 5 1 .8233 4 1 .0042 1 .7229 4 2 373.19 5 1 .8339 4 1 .0042 1 .78 4 2 373.19 5 1 .8399 4 1 .0042 1 .8979 4 2 373.19 5 1 .8673 4 1 .0042 1 .9256 4 2 373.19 5 1 .8811 4 1 .0042 1 .9879 4 2 373.19 5 1 .9642 4 1 .0042 1 .9884 4 2 373.19 5 1 .9648 4 1 .0042 1 .0192 3 2 403.13 5 1 .2475 4 1 .0042 1 .0577 3 2 403.13 5 1 .4689 4 1 .0042 1 .0959 3 2 403.13 5 1 .5884 4 1 .0042 1 .1625 4 2 403.13 5 1 .6646 4 1 .0042 1 .3141 4 2 403.13 5 1 .7154 4 1 .0042 1 .4959 4 2 403.13 5 1 .7395 4 1 .0042 1 .6971 4 2 403.13 5 1 .7746 4 1 .0042 1 .8183 4 2 403.13 5 1 .8072 4 1 .0042 1 .8986 4 2 403.13 5 1 .8552 4 1 .0042 1 .9429 4 2 403.13 5 1 .9042 4 1 .0042 1 .9918 4 2 403.13 5 1 .9821 4 1 .0042 1 .0191 3 2 423.09 5 1 .2258 4 1 .0042 1 .0488 3 2 423.09 5 1 .377 4 1 .0042 1 .1095 4 2 423.09 5 1 .5083 4 1 .0042 1 .1915 4 2 423.09 5 1 .5892 4 1 .0042 1 .3062 4 2 423.09 5 1 .6353 4 1 .0042 1 .5195 4 2 423.09 5 1 .6782 4 1 .0042 1 .7128 4 2 423.09 5 1 .7348 4 1 .0042 1 .0094 2 2 433.16 5 1 .1032 4 1 .0042 1 .0146 3 2 433.16 5 1 .1488 4 1 .0042 1 .0259 3 2 433.16 5 1 .2392 4 1 .0042 1 .0448 3 2 433.16 5 1 .3327 4 1 .0042 1 .0883 3 2 433.16 5 1 .4179 4 1 .0042 1 .0924 3 2 433.16 5 1 .428 4 1 .0042 1 .1559 4 2 433.16 5 1 .5 4 1 .0042 1 .1582 4 2 433.16 5 1 .5124 4 1 .0042 1 .2425 4 2 433.16 5 1 .5572 4 1 .0042 1 .2794 4 2 433.16 5 1 .5658 4 1 .0042 1 .4244 4 2 433.16 5 1 .6146 4 1 .0042 1 .0113 3 2 443.19 5 1 .0666 3 1 .0042 1 .0377 3 2 443.19 5 1 .1976 4 1 .0042 1 .064 3 2 443.19 5 1 .2708 4 1 .0042 1 .0917 3 2 443.19 5 1 .33 4 1 .0042 1 .1515 4 2 443.19 5 1 .4217 4 1 .0042 1 .2299 4 2 443.19 5 1 .471 4 1 .0042 1 .3688 4 2 443.19 5 1 .5044 4 1 .0042