Infer dissolved gas from its own partial-pressure constraint
Solubility is an equilibrium composition under specified conditions.
Learning outcome: Compare(200 kPa,.20) with(100 kPa,.40), then compare fixed total pressure at two fractions. Retain partial pressure and equilibrium concentration; identify the held-fixed temperature and solvent.
Starting recap
Use chemical amount, dimensional ratios and positive interval endpoints. Distinguish original formula units, independently moving species and a chosen thermodynamic standard.
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At total200 kPa and gas solute fraction.20, solute partial pressure40 kPa gives c=2×10⁻5×40=.000800 M.
Open the experimentPredict
Will raising total pressure with an inert gas necessarily raise dissolved solute concentration?
Experiment
Compare(200 kPa,.20) with(100 kPa,.40), then compare fixed total pressure at two fractions. Retain partial pressure and equilibrium concentration; identify the held-fixed temperature and solvent.
Use solute partial pressure rather than total pressure
Worked teaching model · synthetic values · Dilute nonreacting gas at fixed temperature; c=kH*p with supplied kH=2.0×10⁻5 mol/(L kPa). Ideal gas partial pressure yP; equilibrium with a large reservoir. Henry constants have multiple reciprocal conventions; this one has explicitly stated units. No gas dissolution kinetics or pressurized apparatus.
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Axes rescale. Connected samples represent declared equilibrium or activity relationships, not elapsed time. Dashed lines show the concentration-scale gamma=1 reference or ideal Raoult total pressure as named in the model.
Numerical diagram coordinates
| total reservoir pressure (kPa) | equilibrium dissolved solute (mol/L) |
|---|---|
| 0 | 0 |
| 10 | 4.000000e-5 |
| 20 | 8.000000e-5 |
| 30 | 0.00012 |
| 40 | 0.00016 |
| 50 | 0.0002 |
| 60 | 0.00024 |
| 70 | 0.00028 |
| 80 | 0.00032 |
| 90 | 0.00036 |
| 100 | 0.0004 |
| 110 | 0.00044 |
| 120 | 0.00048 |
| 130 | 0.00052 |
| 140 | 0.00056 |
| 150 | 0.0006 |
| 160 | 0.00064 |
| 170 | 0.00068 |
| 180 | 0.00072 |
| 190 | 0.00076 |
| 200 | 0.0008 |
| 210 | 0.00084 |
| 220 | 0.00088 |
| 230 | 0.00092 |
| 240 | 0.00096 |
| 250 | 0.001 |
| 260 | 0.00104 |
| 270 | 0.00108 |
| 280 | 0.00112 |
| 290 | 0.00116 |
| 300 | 0.0012 |
| Quantity | Value | Unit |
|---|---|---|
| Solute partial pressure | 40 | kPa |
| Equilibrium dissolved concentration | 0.0008 | mol/L |
| Incorrect total-pressure inference | 0.004 | mol/L |
Gas identity, temperature and its own partial pressure set the stated equilibrium concentration.
An inert-gas addition at constant solute partial pressure does not change this ideal-dilute prediction, even if total pressure rises. The coefficient is temperature- and solvent-dependent and its reciprocal is also called a Henry constant in other conventions. Stirring changes approach rates, not this equilibrium relation; reactive gases require additional chemistry.
Retain the species, standard state and ideal/nonideal assumptions with every number. This mathematical packet is not a solution-preparation procedure or evidence of observed laboratory technique.
Gas identity, temperature and its own partial pressure set the stated equilibrium concentration.
An inert-gas addition at constant solute partial pressure does not change this ideal-dilute prediction, even if total pressure rises. The coefficient is temperature- and solvent-dependent and its reciprocal is also called a Henry constant in other conventions. Stirring changes approach rates, not this equilibrium relation; reactive gases require additional chemistry.
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Why does faster mixing not prove that an equilibrium solubility constant changed?
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