IUPAC-NIST Solubility Database
NIST Standard Reference Database 106


Glass Ball as Bullet Solubility System: Ethene with Heptane

Components:
   (1) Ethene; C2H4; [74-85-1]  NIST Chemistry WebBook for detail
   (2) Heptane; C7H16; [142-82-5]  NIST Chemistry WebBook for detail

Original Measurements:
   Kay, W.B., Ind. Eng. Chem. 1948, 40, 1459-1464.

Variables:
   Temperature = 211.5 K to 522.0 K
   Pressure = 0.677 to 19.15

Prepared By:
   W. Hayduk

Experimental Data:   (Subscripts 1,2,3, ..., in column headings refer to components 1,2,3, ...)
  
T/KTemp NotePressure [psia]Pressure [MPa]Pressure NoteHenry's law constant, K [y1/x1]Henry Constant NoteMass Fraction (w1)w1 NoteMole Fraction (x1)x1 NoteMole Fraction (x2)x2 Note
357.0411000.689112.9410.0208in Liquid, mass0.0704in liquid12.941 Equilibrium Constant for Ethene y1/x1
399.9311501.034111.3810.0208in Liquid, mass0.0704in liquid11.381 Equilibrium Constant for Ethene y1/x1
431.5412001.37919.8710.0208in Liquid, mass0.0704in liquid9.871 Equilibrium Constant for Ethene y1/x1
455.7612501.72418.6610.0208in Liquid, mass0.0704in liquid8.661 Equilibrium Constant for Ethene y1/x1
475.3713002.06817.7010.0208in Liquid, mass0.0704in liquid7.701 Equilibrium Constant for Ethene y1/x1
492.4313502.41316.8910.0208in Liquid, mass0.0704in liquid6.891 Equilibrium Constant for Ethene y1/x1
507.9314002.75816.1510.0208in Liquid, mass0.0704in liquid6.151 Equilibrium Constant for Ethene y1/x1
522.0414503.10315.5010.0208in Liquid, mass0.0704in liquid5.501 Equilibrium Constant for Ethene y1/x1
275.3711000.68915.4110.0596in Liquid, mass0.1846in liquid5.411 Equilibrium Constant for Ethene y1/x1
303.5911501.03415.3810.0596in Liquid, mass0.1846in liquid5.381 Equilibrium Constant for Ethene y1/x1
328.4312001.37915.3410.0596in Liquid, mass0.1846in liquid5.341 Equilibrium Constant for Ethene y1/x1
351.7112501.72415.2810.0596in Liquid, mass0.1846in liquid5.281 Equilibrium Constant for Ethene y1/x1
374.3713002.06815.1810.0596in Liquid, mass0.1846in liquid5.181 Equilibrium Constant for Ethene y1/x1
395.9313502.41315.0510.0596in Liquid, mass0.1846in liquid5.051 Equilibrium Constant for Ethene y1/x1
416.2614002.75814.9010.0596in Liquid, mass0.1846in liquid4.901 Equilibrium Constant for Ethene y1/x1
435.9814503.10314.7110.0596in Liquid, mass0.1846in liquid4.711 Equilibrium Constant for Ethene y1/x1
454.8715003.44714.5010.0596in Liquid, mass0.1846in liquid4.501 Equilibrium Constant for Ethene y1/x1
473.1515503.79214.2710.0596in Liquid, mass0.1846in liquid4.271 Equilibrium Constant for Ethene y1/x1
491.4316004.13714.0110.0596in Liquid, mass0.1846in liquid4.011 Equilibrium Constant for Ethene y1/x1
515.3716504.48213.5810.0596in Liquid, mass0.1846in liquid3.581 Equilibrium Constant for Ethene y1/x1
252.5911000.68913.5010.1007in Liquid, mass0.2857in liquid3.501 Equilibrium Constant for Ethene y1/x1
273.1511501.03413.5010.1007in Liquid, mass0.2857in liquid3.501 Equilibrium Constant for Ethene y1/x1
290.9312001.37913.4910.1007in Liquid, mass0.2857in liquid3.491 Equilibrium Constant for Ethene y1/x1
307.5412501.72413.4910.1007in Liquid, mass0.2857in liquid4.591 Equilibrium Constant for Ethene y1/x1
323.2613002.06813.4810.1007in Liquid, mass0.2857in liquid3.481 Equilibrium Constant for Ethene y1/x1
338.5913502.41313.4610.1007in Liquid, mass0.2857in liquid3.461 Equilibrium Constant for Ethene y1/x1
353.5414002.75813.4510.1007in Liquid, mass0.2857in liquid3.451 Equilibrium Constant for Ethene y1/x1
368.2614503.10313.4210.1007in Liquid, mass0.2857in liquid3.421 Equilibrium Constant for Ethene y1/x1
383.2115003.44713.4010.1007in Liquid, mass0.2857in liquid3.401 Equilibrium Constant for Ethene y1/x1
398.2615503.79213.3610.1007in Liquid, mass0.2857in liquid3.361 Equilibrium Constant for Ethene y1/x1
413.4816004.13713.3210.1007in Liquid, mass0.2857in liquid3.321 Equilibrium Constant for Ethene y1/x1
428.9816504.48213.2610.1007in Liquid, mass0.2857in liquid3.261 Equilibrium Constant for Ethene y1/x1
444.8217004.82613.1910.1007in Liquid, mass0.2857in liquid3.191 Equilibrium Constant for Ethene y1/x1
462.0417505.17113.1110.1007in Liquid, mass0.2857in liquid3.111 Equilibrium Constant for Ethene y1/x1
483.8718005.51612.9710.1007in Liquid, mass0.2857in liquid2.971 Equilibrium Constant for Ethene y1/x1
300.0914002.75812.11410.2005in Liquid, mass0.4725in liquid2.1141 Equilibrium Constant for Ethene y1/x1
308.8214503.10312.11310.2005in Liquid, mass0.4725in liquid2.1131 Equilibrium Constant for Ethene y1/x1
317.2615003.44712.11210.2005in Liquid, mass0.4725in liquid2.1121 Equilibrium Constant for Ethene y1/x1
325.4815503.79212.11010.2005in Liquid, mass0.4725in liquid2.1101 Equilibrium Constant for Ethene y1/x1
333.7116004.13712.10910.2005in Liquid, mass0.4725in liquid2.1091 Equilibrium Constant for Ethene y1/x1
341.9316504.48212.10710.2005in Liquid, mass0.4725in liquid2.1071 Equilibrium Constant for Ethene y1/x1
350.0917004.82612.10410.2005in Liquid, mass0.4725in liquid2.1041 Equilibrium Constant for Ethene y1/x1
358.7117505.17112.10110.2005in Liquid, mass0.4725in liquid2.1011 Equilibrium Constant for Ethene y1/x1
367.2118005.51612.09810.2005in Liquid, mass0.4725in liquid2.0981 Equilibrium Constant for Ethene y1/x1
375.9318505.86112.09410.2005in Liquid, mass0.4725in liquid2.0941 Equilibrium Constant for Ethene y1/x1
385.0919006.20512.08910.2005in Liquid, mass0.4725in liquid2.0891 Equilibrium Constant for Ethene y1/x1
394.6519506.55012.08310.2005in Liquid, mass0.4725in liquid2.0831 Equilibrium Constant for Ethene y1/x1
404.82110006.89512.07610.2005in Liquid, mass0.4725in liquid2.0761 Equilibrium Constant for Ethene y1/x1
415.48110507.23912.06710.2005in Liquid, mass0.4725in liquid2.0671 Equilibrium Constant for Ethene y1/x1
427.59111007.58412.03110.2005in Liquid, mass0.4725in liquid2.0311 Equilibrium Constant for Ethene y1/x1
445.93111507.92912.03110.2005in Liquid, mass0.4725in liquid2.0311 Equilibrium Constant for Ethene y1/x1
Notes:
   1  Calculated by compiler. Raoult's law was used to calculate the vapor composition and K, both being approximations.

Method/Apparatus/Procedure:
   Heptane was charged into the high pressure cell, degassed, and its quantity determined by volume. A measured volume of ethene gas was added from a storage bomb at constant temperature to give a known liquid composition by a material balance. The liquid composition was considered to remain constant for the changes in temperature and pressure involved in each series of experiments because of the small gas volume used. Densities and critical properties of the solutions were also given at high pressure. Details of experimental method given in Ref. 1.
Vapor-liquid equilibria for eight ethene compositions are reported. The results for four of the compositions, in which the mole fractions are less than 0.5, may be considered solubility equilibria and are listed here.

Source and Purity of Materials:
   1. Commercial high purity ethene was fractionated then degassed by repeated freezing, evacuation and melting. Actual purity not indicated.
   2. Heptane purity not specified.

Estimated Errors:
   Solubility: δx1/x1 = ± 0.03 (compiler)
   Temperature: δT/K = ± 0.02
   Pressure: δP/P = ± 0.005

References:
   1. Kay, W.B., Ind. Eng. Chem. 1938, 30, 459.