SDS Volume (2838)

Volume 62. Carbon Dioxide in Water and Aqueous Electrolyte Solutions, p None

Original Measurements

Rumpf, B.; Maurer, G.; Ber. Bunsenges. Phys. Chem. 1993, 97, 85-97.

Variables:

Room Temp: 313.13 - 433.18 $\pu{K}$
Pressure: 0.0181 - 9.868 $\pu{MPa}$
Molality (2): m2/mol kg-1 = near 2.00 and 4.00 mol/kg

Prepared by:

H.L. Clever

Method/Apparatus/Procedure:

The apparatus is a modification of one used in earlier work [1]. It consists of a high pressure optical cell, thermostat, magnetic stirrer, thermocouples and $\ce{Pt}$ resistance thermometer, pressure transducers and tanks for aqueous solutions, rinse water and solute gas. The thermostatted about 30 mL high pressure optical cell is filled with carbon dioxide. Pressure and temperature of the gas are measured after equilibration. A known amount of aqueous solvent is added which is slightly greater than that needed to completely dissolve the gas. The pressure in the cell is reduced step-wise by removing very small amounts of the liquid until the first stable bubble appears. The mass of carbon dioxide is calculated from the Bender equation (2). The volume of the cell is known within 0.06 mL. The solvent density is from the literature.

Source and Purity of Materials:
  1. Carbon dioxide. Messer Griesheim, Ludwigshafen, > 99.995 mol%, used as received.
  2. Ammonium sulfate. Merck GmbH, Darmstadt, > 99.5 mass%. Degassed and dried under vacuum.
  3. Water. Deionized and degassed by vacuum distillation.
Estimated Errors:

Ambient temperature: δT/K = ±0.1
Mass concentration (m/v) (1): δm2/m2 = ±0.003
δm1/m1 = ±0.1 to 0.03

References

1 Rumpf, B.; Maurer, G.; Fluid Phase Equilib. 1992, 81, 241-60.
2 Bender, E.; 5th Proc. Symp. Thermophys. Prop., ASME, NY, 1970, 227-35.

Components:
  1. Carbon dioxide, $\ce{ CO2 }$; [124-38-9] NIST WebBook
  2. Ammonium sulfate, $\ce{ (NH4)2SO4 }$; [7783-20-2] NIST WebBook
  3. Water, $\ce{ H2O }$; [7732-18-5] NIST WebBook
Experimental Data

The authors used Pitzer's semiempirical model to correlate the data. The dissociation of the carbon dioxide can be neglected at the concentrations here. The system was treated as containing a non-dissociating gas, G and a completely dissociating electrolyte, MX. A temperature dependent interaction parameter, B°CO2, (NH4)2SO4, and a temperature independent interaction parameter, ΓCO2, (NH4)2SO4, (NH4)2SO4, were derived from the experimental data.

For the CO2 + (NH4)2SO4 + H2O system the values are:
CO2, (NH4)2SO4 = 0.7790 - 446.7(T/K)-1 + 78900(T/K)-2

which gives values:

T/K
313.15 353.15 393.15 433.15
CO2, (NH4)2SO4
0.1571 0.1467 0.1533 0.1683

and ΓCO2, (NH4)2SO4, (NH4)2SO4 = - 0.0083.

Solubility of carbon dioxide in aqueous ammonium sulfate
$T$ ($\pu{K}$) m1 (mol/kg) m2 (mol/kg) $P$ ($\pu{MPa}$)
313.15 0.05372.0150.4060
313.15 0.08082.0150.626
313.14 0.19922.0151.594
313.14 0.30752.0152.545
313.15 0.41042.0153.607
313.13 0.51302.0154.783
313.13 0.62102.0156.370
313.13 0.70732.0158.104
313.16 0.72722.0158.968
313.16 0.06463.9890.707
313.14 0.10613.9891.138
313.15 0.20053.9892.235
313.14 0.30093.9893.619
313.14 0.40213.9895.294
313.13 0.50223.9897.716
313.15 0.54533.9898.966
333.13 0.02.0000.0185
333.15 0.04942.0150.518
333.16 0.09882.0151.086
333.15 0.20082.0152.297
333.13 0.30162.0153.618
333.15 0.39842.0155.075
333.14 0.49932.0156.876
333.13 0.55112.0157.965
333.14 0.59832.0159.346
333.13 0.03.9340.0181
333.15 0.05843.9890.796
333.13 0.10063.9891.420
333.15 0.20093.9893.114
333.15 0.30133.9895.138
333.16 0.40323.9897.789
333.18 0.44823.9899.395
353.10 0.01.9990.0445
353.15 0.04952.0150.715
353.19 0.10022.0151.437
353.15 0.20082.0152.992
353.15 0.30252.0154.720
353.15 0.40232.0156.775
353.15 0.45242.0157.991
353.15 0.50122.0159.343
353.15 0.03.9340.0420
353.16 0.05173.9890.885
353.14 0.10123.9891.848
353.14 0.20133.9894.096
353.15 0.25183.9895.428
353.14 0.30223.9896.879
353.14 0.35343.9898.540
353.14 0.37853.9899.512
393.16 0.02.0050.1778
393.16 0.05062.0051.057
393.16 0.08752.0051.770
393.16 0.10052.0152.080
393.18 0.13772.0052.768
393.16 0.20072.0154.185
393.16 0.23972.0054.950
393.16 0.30102.0056.456
393.16 0.33752.0057.483
393.15 0.34852.0057.739
393.16 0.39072.0058.848
393.16 0.03.9890.1705
393.09 0.4963.9891.363
393.15 0.10093.9892.757
393.14 0.15163.9894.198
393.15 0.20303.9895.905
393.15 0.25313.9897.743
393.14 0.30423.9899.764
413.11 0.01.9820.337
413.15 0.4992.0051.291
413.15 0.07542.0051.808
413.15 0.10062.0052.327
413.16 0.20052.0054.526
413.15 0.30132.0056.905
413.16 0.30122.0056.975
413.15 0.35192.0058.397
413.15 0.40212.0059.868
413.20 0.04.0130.317
413.21 0.48894.0131.627
413.11 0.10043.9893.214
413.08 0.14993.9894.747
413.14 0.20163.9896.621
413.21 0.24134.0138.294
413.08 0.24983.9898.580
413.20 0.25924.0139.047
433.15 0.02.0050.572
433.14 0.05082.0051.594
433.14 0.10062.0052.689
433.12 0.15132.0053.827
433.14 0.20122.0055.010
433.10 0.25212.0056.297
433.14 0.30142.0057.580
433.12 0.35392.0059.011
433.14 0.37822.0059.751
433.15 0.04.0130.546
433.15 0.04624.0131.986
433.14 0.09214.0133.470
433.16 0.13824.0135.036
433.15 0.17514.0136.350
433.16 0.20094.0137.361
433.18 0.22564.0138.312
433.10 0.25104.0139.372

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