Interpret nonideal gas evidence without a single-cause shortcut
Separate two model corrections and test the domain before interpreting compressibility.
Learning outcome: Compare300 and 500 K at Vm1, then vary volume at fixed temperature . Retain each correction, total pressure and Z; verify Vm>b and the declared above-critical boundary.
Starting recap
Review amount dimensions, chemical formulas and charge, signed differences, ratio bounds and the distinction between a theoretical constraint and measured conversion.
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Try
At Vm=1 L/mol,T=350 K, ideal pressure is 2909.9 kPa; excluded volume adds153.153 and attraction subtracts200, giving2863.053 kPa and Z≈.98390.
Open the experimentPredict
Does Z close to 1 prove that intermolecular interactions are absent?
Experiment
Compare300 and 500 K at Vm1, then vary volume at fixed temperature . Retain each correction, total pressure and Z; verify Vm>b and the declared above-critical boundary.
Compare attractive and excluded-volume corrections
Worked teaching model · synthetic values · Fictional van der Waals gas with a=200 kPa L²/mol² and b=0.050 L/mol: P=RT/(Vm−b)−a/Vm², R=8.314. Selected T exceeds this model critical temperature8a/(27Rb)≈142.6 K and Vm exceeds b. Positive-pressure single-phase comparison; not a real gas property fit or pressure-system design.
Reset keeps your prediction, captures and practice history.
Axes rescale. Connected samples show a declared parameter relationship, not elapsed reaction time. Dashed comparison, when present, is the unbiased gas pressure or ideal-gas Z=1 reference described in the model.
Numerical diagram coordinates
| molar volume (L/mol) | compressibility Z |
|---|---|
| 0.5 | 0.9736493 |
| 0.625 | 0.9769871 |
| 0.75 | 0.9797874 |
| 0.875 | 0.9820565 |
| 1 | 0.9839007 |
| 1.125 | 0.9854175 |
| 1.25 | 0.986682 |
| 1.375 | 0.9877498 |
| 1.5 | 0.9886622 |
| 1.625 | 0.9894501 |
| 1.75 | 0.990137 |
| 1.875 | 0.9907408 |
| 2 | 0.9912756 |
| 2.125 | 0.9917524 |
| 2.25 | 0.9921802 |
| 2.375 | 0.9925661 |
| 2.5 | 0.9929158 |
| 2.625 | 0.9932343 |
| 2.75 | 0.9935255 |
| 2.875 | 0.9937927 |
| 3 | 0.9940389 |
| molar volume (L/mol) | compressibility Z |
|---|---|
| 0.5 | 1 |
| 0.625 | 1 |
| 0.75 | 1 |
| 0.875 | 1 |
| 1 | 1 |
| 1.125 | 1 |
| 1.25 | 1 |
| 1.375 | 1 |
| 1.5 | 1 |
| 1.625 | 1 |
| 1.75 | 1 |
| 1.875 | 1 |
| 2 | 1 |
| 2.125 | 1 |
| 2.25 | 1 |
| 2.375 | 1 |
| 2.5 | 1 |
| 2.625 | 1 |
| 2.75 | 1 |
| 2.875 | 1 |
| 3 | 1 |
| Quantity | Value | Unit |
|---|---|---|
| Ideal pressure | 2909.9 | kPa |
| Excluded-volume pressure correction | 153.1526 | kPa |
| Attractive pressure correction | -200 | kPa |
| Model pressure | 2863.053 | kPa |
| Compressibility factor | 0.9839007 | ratio |
| Model critical temperature | 142.5529 | K |
| Available molar volume | 0.95 | L/mol |
Attraction lowers and excluded volume raises the pressure relative to the ideal model at fixed T and Vm.
The two corrections compete; Z near1 can reflect cancellation rather than absence of interactions. The bounded domain stays above the stipulated critical temperature with positive pressure and Vm>b. This fictional equation is not an empirical fit to a named gas or a description of liquid–vapor coexistence.
Retain the reaction/measurement boundary with every number. This mathematical packet is not a chemical procedure or evidence of actual laboratory technique.
Attraction lowers and excluded volume raises the pressure relative to the ideal model at fixed T and Vm.
The two corrections compete; Z near1 can reflect cancellation rather than absence of interactions. The bounded domain stays above the stipulated critical temperature with positive pressure and Vm>b. This fictional equation is not an empirical fit to a named gas or a description of liquid–vapor coexistence.
Captures preserve recipes and replay their calculated results. They are synthetic model evidence, not physical measurements.
Understand
Apply
Public practice checks a specific claim. It does not establish independent mastery.
Why is an apparently good Z value not a unique fit of a real gas mechanism?
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