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IUPAC-NIST Solubility Database
NIST Standard Reference Database 106
Solubility System:
Nitromethane with 1,2-Ethanediol-d2
Components:
(1) Nitromethane; CH3NO2; [75-52-5]
NIST Chemistry WebBook
for detail
(2) 1,2-Ethanediol-d2; C2D2H4O2; [7782-39-0]
NIST Chemistry WebBook
for detail
Original Measurements:
Salvi, M.V.; Van Hook, W.A., J. Phys. Chem. 94, 7812 (1990).
Variables:
Temperature = 313 K to 316 K
Pressure = 313 K to 316 K
Prepared By:
V. P. Sazonov
Experimental Remarks:
UCST at
P
= 0.1 MPa is 315.04 K at x
1
= 0.642 (100 w
1
= 63.1, compiler).
(d
T
c
/d
P
) = (1.60 ± 0.04) · 10
-2
K · MPa
-1
.
Experimental Data:
(Notes on the Nomenclature)
t/°C
T/K
Pressure [Mpa]
Mass Fraction w
1
(compiler)
w1 Compiler Note
Mole Fraction x
1
Comment(s)
39.959
313.109
0.1400
48.60
2
0.4981
Glycol-rich phase
39.959
313.109
0.1400
-
2
-
Nitromethane-rich phase
40.234
313.384
0.1100
-
2
-
Glycol-rich phase
40.234
313.384
0.1100
77.61
2
0.7844
Nitromethane-rich phase
40.501
313.651
0.1100
50.60
2
0.5181
Glycol-rich phase
40.501
313.651
0.1100
-
2
-
Nitromethane-rich phase
41.481
314.631
0.1200
-
2
-
Glycol-rich phase
41.481
314.631
0.1200
69.31
2
0.7041
Nitromethane-rich phase
41.553
314.703
0.5700
58.75
2
0.5992
Glycol-rich phase
41.553
314.703
0.5700
-
2
-
Nitromethane-rich phase
41.881
315.031
0.1200
-
2
-
Glycol-rich phase
41.881
315.031
0.1200
64.28
2
0.6539
Nitromethane-rich phase
40.000
313.150
2.510
48.60
2
0.4981
Glycol-rich phase
40.000
313.150
2.510
-
2
-
Nitromethane-rich phase
40.274
313.424
2.690
-
2
-
Glycol-rich phase
40.274
313.424
2.690
77.61
2
0.7844
Nitromethane-rich phase
40.544
313.694
2.520
50.60
2
0.5181
Glycol-rich phase
40.544
313.694
2.520
-
2
-
Nitromethane-rich phase
41.499
314.649
1.700
-
2
-
Glycol-rich phase
41.499
314.649
1.700
69.31
2
0.7041
Nitromethane-rich phase
41.921
315.071
2.500
62.41
2
0.6354
Glycol-rich phase
41.921
315.071
2.500
-
2
-
Nitromethane-rich phase
41.426
314.576
5.810
58.75
2
0.5992
Glycol-rich phase
41.426
314.576
5.810
-
2
-
Nitromethane-rich phase
41.554
314.704
5.030
-
2
-
Glycol-rich phase
41.554
314.704
5.030
69.31
2
0.7041
Nitromethane-rich phase
41.960
315.110
5.070
62.41
2
0.6354
Glycol-rich phase
41.960
315.110
5.070
-
2
-
Nitromethane-rich phase
40.062
313.212
10.11
48.60
2
0.4981
Glycol-rich phase
40.062
313.212
10.11
-
2
-
Nitromethane-rich phase
40.398
313.548
10.07
-
2
-
Glycol-rich phase
40.398
313.548
10.07
77.61
2
0.7844
Nitromethane-rich phase
40.598
313.748
9.880
50.60
2
0.5181
Glycol-rich phase
40.598
313.748
9.880
-
2
-
Nitromethane-rich phase
41.475
314.625
10.98
58.75
2
0.5992
Glycol-rich phase
41.475
314.625
10.98
-
2
-
Nitromethane-rich phase
41.610
314.760
10.10
-
2
-
Glycol-rich phase
41.610
314.760
10.10
69.31
2
0.7041
Nitromethane-rich phase
42.011
315.161
9.930
62.41
2
0.6354
Glycol-rich phase
42.011
315.161
9.930
-
2
-
Nitromethane-rich phase
40.150
313.300
14.74
48.60
2
0.4981
Glycol-rich phase
40.150
313.300
14.74
-
2
-
Nitromethane-rich phase
40.484
313.634
14.74
-
2
-
Glycol-rich phase
40.484
313.634
14.74
77.61
2
0.7844
Nitromethane-rich phase
40.570
313.720
15.03
-
2
-
Glycol-rich phase
40.570
313.720
15.03
69.31
2
0.7041
Nitromethane-rich phase
40.160
313.310
20.01
48.60
2
0.4981
Glycol-rich phase
40.160
313.310
20.01
-
2
-
Nitromethane-rich phase
40.680
313.830
20.01
50.60
2
0.5181
Glycol-rich phase
40.680
313.830
20.01
-
2
-
Nitromethane-rich phase
41.580
314.730
20.03
58.75
2
0.5992
Glycol-rich phase
41.580
314.730
20.03
-
2
-
Nitromethane-rich phase
41.736
314.886
20.02
-
2
-
Glycol-rich phase
41.736
314.886
20.02
69.31
2
0.7041
Nitromethane-rich phase
40.284
313.434
29.98
48.60
2
0.4981
Glycol-rich phase
40.284
313.434
29.98
-
2
-
Nitromethane-rich phase
40.717
313.867
30.31
-
2
-
Glycol-rich phase
40.717
313.867
30.31
77.61
2
0.7844
Nitromethane-rich phase
40.838
313.988
31.32
50.60
2
0.5181
Glycol-rich phase
40.838
313.988
31.32
-
2
-
Nitromethane-rich phase
41.744
314.894
30.04
58.75
2
0.5992
Glycol-rich phase
41.744
314.894
30.04
-
2
-
Nitromethane-rich phase
41.866
315.016
30.05
-
2
-
Glycol-rich phase
41.866
315.016
30.05
69.31
2
0.7041
Nitromethane-rich phase
40.795
313.945
35.06
-
2
-
Glycol-rich phase
40.795
313.945
35.06
77.61
2
0.7844
Nitromethane-rich phase
40.289
313.539
40.05
48.60
2
0.4981
Glycol-rich phase
40.289
313.539
40.05
-
2
-
Nitromethane-rich phase
40.924
314.074
40.93
50.60
2
0.5181
Glycol-rich phase
40.924
314.074
40.93
-
2
-
Nitromethane-rich phase
41.993
315.143
40.00
-
2
-
Glycol-rich phase
41.993
315.143
40.00
69.31
2
0.7041
Nitromethane-rich phase
42.053
315.203
40.13
58.75
2
0.5992
Glycol-rich phase
42.053
315.203
40.13
-
2
-
Nitromethane-rich phase
42.184
315.334
40.11
-
2
-
Glycol-rich phase
42.184
315.334
40.11
64.28
2
0.6539
Nitromethane-rich phase
40.433
313.583
44.86
48.60
2
0.4981
Glycol-rich phase
40.433
313.583
44.86
-
2
-
Nitromethane-rich phase
40.957
314.107
45.03
-
2
-
Glycol-rich phase
40.957
314.107
45.03
77.61
2
0.7844
Nitromethane-rich phase
40.510
313.660
50.08
48.60
2
0.4981
Glycol-rich phase
40.510
313.660
50.08
-
2
-
Nitromethane-rich phase
41.074
314.224
50.05
50.60
2
0.5189
Glycol-rich phase
41.074
314.224
50.05
-
2
-
Nitromethane-rich phase
42.133
315.283
50.01
-
2
-
Glycol-rich phase
42.133
315.283
50.01
69.31
2
0.7041
Nitromethane-rich phase
42.185
315.335
50.16
58.75
2
0.5992
Glycol-rich phase
42.185
315.335
50.16
-
2
-
Nitromethane-rich phase
42.335
315.505
50.03
-
2
-
Glycol-rich phase
42.335
315.505
50.03
64.28
2
0.6539
Nitromethane-rich phase
Method/Apparatus/Procedure:
The synthetic method was used. Measurements were made using techniques and apparatus described in Ref. 1 with minor modification. Mixtures of (1) and (2) were prepared gravimetrically. The solutions were degassed with a series of freeze-pump (≤0.1 Pa) - thaw cycles. After transfer to the apparatus (previously warmed above the CST) the demixing was determined by allowing the mixture to cool to the transition temperature at a rate of (3 to 5) mK/min while stirring. Temperature was measured by platinum resistance thermometry.
Source and Purity of Materials:
(1) Mallinkrodt; analytical grade; dried over anhydrous CaCl
2
and twice distilled in a spinning band column below 343 K.
(2) Prepared by refluxing reagent grade 99.8 % D
2
O/ethanediol = 2.5/1 and removing the water by fractional distillation at reduced pressure; the deuterated glycol fraction was collected, dried again over molecular sieve and redistilled.
Estimated Errors:
Temperature: ± 0.3 mK.
Pressure: ±0.01MPa.
References:
1
R. R. Singh and W. A. Van Hook, J. Chem. Phys. 87, 6097 (1987).