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IUPAC-NIST Solubility Database
NIST Standard Reference Database 106
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:
Shenderei, E.R.; Ivanovskii, F.P., Khim. Prom. 1963, 91, 18-37.
Variables:
Temperature = 228.15 K to 248.15 K
Pressure = 0.552 to 1.663
Prepared By:
W. Hayduk
Experimental Remarks:
Henry's constant determined for pressures below atmospheric. Graphs given for low pressure range showing that Henry's law is obeyed.
T
/K 228.15 238.15 248.15
H
/Atm(mole fraction)
1
13.5 17.2 20.9
Experimental Data:
(Subscripts 1,2,3, ..., in column headings refer to components 1,2,3, ...)
t/°C
T/K
Pressure [MPa]
Pressure Note
Pressure [Atm]
Mole Fraction (x
1
)
Solubility [cm
3
(STP)/g]
−25
248.15
0.552
1
5.45
0.2376
69.06
−25
248.15
0.556
1
5.49
0.2561
76.26
−25
248.15
0.876
1
8.65
0.3789
135.16
−25
248.15
0.902
1
8.90
0.4091
153.44
−25
248.15
1.033
1
10.19
0.4686
195.37
−25
248.15
1.382
1
13.64
0.6169
356.80
−25
248.15
1.493
1
14.73
0.6834
478.25
−25
248.15
1.597
1
15.76
0.7196
568.00
−25
248.15
1.663
1
16.41
0.7657
723.96
−35
238.15
0.551
1
5.44
0.3085
98.84
−35
238.15
0.561
1
5.54
0.3170
102.85
−35
238.15
0.786
1
7.76
0.4572
186.62
−35
238.15
0.867
1
8.56
0.4909
213.97
−35
238.15
1.305
1
12.88
0.7747
766.11
−35
238.15
1.309
1
12.92
0.7649
721.04
−35
238.15
1.425
1
14.06
0.8550
1305.30
−35
238.15
1.441
1
14.22
0.8539
1294.80
−35
238.15
1.504
1
14.84
0.8945
1877.70
−45
228.15
0.496
1
4.90
0.3636
126.58
−45
228.15
0.528
1
5.21
0.3765
133.80
−45
228.15
0.525
1
5.18
0.3742
132.50
−45
228.15
0.765
1
7.55
0.5742
298.76
−45
228.15
0.794
1
7.84
0.5929
322.74
−45
228.15
0.797
1
7.87
0.5962
324.24
−45
228.15
1.033
1
10.19
0.8161
981.15
−45
228.15
1.043
1
10.29
0.8218
1022.30
−45
228.15
1.069
1
10.55
0.8413
1176.70
−45
228.15
1.111
1
10.96
0.8908
1806.70
−45
228.15
1.132
1
11.17
0.9012
2024.69
Notes:
1
Calculated by compiler. Henry's constant determined for pressure below atmospheric.
Method/Apparatus/Procedure:
The apparatus utilized an absorption tube with a magnetic stirrer. The temperature controlled bath had two compartments, one containing methanol solution, the other containing solid dry ice in acetone. The walls of the vessels served as the heat transfer medium. Capillary tubing connected the absorber to pressure devices, gas and solvent vessels and a vacuum system. A known amount of solvent was charged into the absorber and the quantity of gas was determined by pressure difference in the gas supply vessel.
Source and Purity of Materials:
1. Purified and analyzed by GC. Actual purity not given.
2. Not given.
Estimated Errors:
Solubility: δ
x
1
/x
1
= ± 2% (compiler)
Temperature: δ
T
/K = ± 0.1
References:
1. Shenderei, E.R.; Zelvenski, Ya.D.; Ivanovskii, F.P., Khim. Prom. 1960, 5, 370.