Home
Introduction
Search Menu
IUPAC Series (PDF)
Reference
Version History
About the Project
Disclaimer
Contact Us
Acknowledgements
IUPAC-NIST Solubility Database
NIST Standard Reference Database 106
Solubility System:
Carbon dioxide with Ammonium nitrate and Water
Components:
(1) Ammonium nitrate; NH4NO3; [6484-52-2]
NIST Chemistry WebBook
for detail
(2) Carbon dioxide; CO2; [124-38-9]
NIST Chemistry WebBook
for detail
(3) Water; H2O; [7732-18-5]
NIST Chemistry WebBook
for detail
Original Measurements:
Gerecke, J., Diss. Dr. rer. Nat. 1969, Hochsch. "Carl Schorlemmer", Leuna-Merseburg, DDR.
Variables:
Temperature = 288.15 K to 328.15 K
Pressure = 288.15 K to 328.15 K
Concentration =
c
2
/mol dm
-3
= 0 - 4
Prepared By:
D.M. Mason
Experimental Data:
(Subscripts 1,2,3, ..., in column headings refer to components 1,2,3, ...)
t/°C
T/K
Concentration C
2
[mol/dm
3
]
Keunen coefficient, S
S Note
α
α Note
15
288.15
0
-
b
0.990
a
15
288.15
0.25
-
b
0.969
a
15
288.15
0.5
0.977
b
0.953
a
15
288.15
1
0.944
b
0.907
a
15
288.15
2
0.872
b
0.787
a
15
288.15
4
0.809
b
0.648
a
20
293.15
0
-
b
0.860
a
20
293.15
0.25
-
b
0.858
a
20
293.15
0.5
0.860
b
0.847
a
20
293.15
1
0.834
b
0.799
a
20
293.15
2
0.769
b
0.693
a
20
293.15
4
0.691
b
0.562
a
25
298.15
0
-
b
0.758
a
25
298.15
0.25
-
b
0.747
a
25
298.15
0.5
0.758
b
0.737
a
25
298.15
1
0.743
b
0.711
a
25
298.15
2
0.688
b
0.618
a
25
298.15
4
0.615
b
0.490
a
30
303.15
0
-
b
0.671
a
30
303.15
0.25
-
b
0.662
a
30
303.15
0.5
0.665
b
0.646
a
30
303.15
1
0.663
b
0.634
a
30
303.15
2
0.625
b
0.560
a
30
303.15
4
0.545
b
0.434
a
35
308.15
0
-
b
0.605
a
35
308.15
0.25
-
b
0.587
a
35
308.15
0.5
0.581
b
0.564
a
35
308.15
1
0.591
b
0.564
a
35
308.15
2
0.568
b
0.509
a
35
308.15
4
0.462
b
0.367
a
40
313.15
0
-
b
0.546
a
40
313.15
0.25
-
b
0.525
a
40
313.15
0.5
0.522
b
0.506
a
40
313.15
1
0.511
b
0.496
a
40
313.15
2
0.517
b
0.462
a
40
313.15
4
0.406
b
0.321
a
45
318.15
0
-
b
0.482
a
45
318.15
0.25
-
b
0.471
a
45
318.15
0.5
0.469
b
0.454
a
45
318.15
1
0.477
b
0.453
a
45
318.15
2
0.483
b
0.431
a
45
318.15
4
0.356
b
0.281
a
50
323.15
0
-
b
0.436
a
50
323.15
0.25
-
b
0.430
a
50
323.15
0.5
0.432
b
0.418
a
50
323.15
1
0.419
b
0.407
a
50
323.15
2
0.438
b
0.390
a
50
323.15
4
0.314
b
0.248
a
55
328.15
0
-
b
0.392
a
55
328.15
0.25
-
b
0.389
a
55
328.15
0.5
0.392
b
0.379
a
55
328.15
1
0.387
b
0.367
a
55
328.15
2
0.395
b
0.355
a
55
328.15
4
0.290
b
0.228
a
Notes:
a
α = Bunsen coefficient [cm
3
(STP) cm
-3
atm
-1
].
b
S
= Kuenen coefficient [cm
3
(STP) g
-1
(H
2
O) atm
-1
].
Method/Apparatus/Procedure:
The principle of the Ostwald method was used in which a measured volume of gas-free liquid is stirred in the presence of the gas, and its decrease in volume is measured in a burette over mercury. The volume of liquid was measured at the experimental temperature. For calculation of the Kuenen coefficient, the density of the solution was obtained from Landolt-Börnstein extant 1969. The molar concentration of salt in the liquid was standardized at 20°C. These data are analyzed and discussed further in Ref. 1.
Source and Purity of Materials:
(1)VEB Leuna Works; 99.8 vol %; the impurity was mostly water (author).
(2) DDR pro analysis grade by DDR Standard TGL 5021.
(3) Double distilled.
Estimated Errors:
Temperature: Not given.
References:
1. Gerecke, J.; Bittrich, H.J., Wiss. Z. Tech. Hochsch. Chem. "Carl Schorlemmer" Leuna-Merseburg 1971, 13(2), 115-22.