Close a finite reaction without counting heat and work twice
A favorable reaction is not a promise of full conversion, rapid approach or delivered electrical energy.
Learning outcome: Compare two K values at the same total rate coefficient and two initial totals at fixed K. Retain concentration, extent, heat, Gibbs-excess decrease and hypothetical charge ceilings with their distinct assumptions.
Starting recap
Reconstruct species, calibration, equilibrium, rate and thermodynamic boundaries before combining evidence.
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At total .060 M and K3, equilibrium B is .045 M. With kf+kr=.100 s⁻¹, after10 s B=.045(1−e⁻¹)=.0284454 M. In .050 L the extent is .00142227 mol and the supplied constant-pressure reaction heat is−28.4454 J.
Open the experimentPredict
Does reaching90% of the equilibrium B amount mean90% of initial A has converted?
Experiment
Compare two K values at the same total rate coefficient and two initial totals at fixed K. Retain concentration, extent, heat, Gibbs-excess decrease and hypothetical charge ceilings with their distinct assumptions.
Reconcile finite reaction, relaxation and work availability
Worked teaching model · synthetic values · Fictional ideal dilute A⇌B at298.15 K and constant pressure, volume .050 L; conserved total concentration, initially pure A. Reversible first-order relaxation has kf+kr=.100 s⁻¹ and kf/kr=K. Supplied reaction enthalpy−20 kJ/mol. Ideal-solution chemical Gibbs excess uses concentrations normalized to same equilibrium reference; The disclosed kinetic heat account assumes only pressure-volume work; no physical process instructions. Hypothetical two-electron product recovery gives only a charge ceiling, not guaranteed usable electrical work.
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- B concentration approaching finite equilibrium: solid
Axes rescale. A compatible-parameter family is not a time trajectory. Read each axis and do not treat a computed curve as additional measured evidence.
All calculated plot coordinates
| time (s) | B concentration (mol/L) |
|---|---|
| 0 | 0 |
| 1 | 0.004282316 |
| 2 | 0.008157116 |
| 3 | 0.01166318 |
| 4 | 0.0148356 |
| 5 | 0.01770612 |
| 6 | 0.02030348 |
| 7 | 0.02265366 |
| 8 | 0.0247802 |
| 9 | 0.02670437 |
| 10 | 0.02844543 |
| 11 | 0.0300208 |
| 12 | 0.03144626 |
| 13 | 0.03273607 |
| 14 | 0.03390314 |
| 15 | 0.03495914 |
| 16 | 0.03591466 |
| 17 | 0.03677924 |
| 18 | 0.03756155 |
| 19 | 0.03826941 |
| 20 | 0.03890991 |
| 21 | 0.03948946 |
| 22 | 0.04001386 |
| 23 | 0.04048835 |
| 24 | 0.04091769 |
| 25 | 0.04130618 |
| 26 | 0.04165769 |
| 27 | 0.04197575 |
| 28 | 0.04226355 |
| 29 | 0.04252396 |
| 30 | 0.04275958 |
| 31 | 0.04297279 |
| 32 | 0.0431657 |
| 33 | 0.04334026 |
| 34 | 0.0434982 |
| 35 | 0.04364112 |
| 36 | 0.04377043 |
| 37 | 0.04388744 |
| 38 | 0.04399332 |
| 39 | 0.04408911 |
| 40 | 0.0441758 |
| 41 | 0.04425423 |
| 42 | 0.0443252 |
| 43 | 0.04438941 |
| 44 | 0.04444752 |
| 45 | 0.0445001 |
| 46 | 0.04454767 |
| 47 | 0.04459071 |
| 48 | 0.04462966 |
| 49 | 0.0446649 |
| 50 | 0.04469679 |
| 51 | 0.04472565 |
| 52 | 0.04475175 |
| 53 | 0.04477538 |
| 54 | 0.04479675 |
| 55 | 0.0448161 |
| 56 | 0.0448336 |
| 57 | 0.04484943 |
| 58 | 0.04486376 |
| 59 | 0.04487672 |
| 60 | 0.04488846 |
| Quantity | Value | Unit |
|---|---|---|
| Equilibrium B concentration | 0.045 | mol/L |
| B concentration after10 s | 0.02844543 | mol/L |
| Forward rate coefficient | 0.075 | s⁻¹ |
| Reverse rate coefficient | 0.025 | s⁻¹ |
| Time to90% of equilibrium B | 23.02585 | s |
| Reaction extent after10 s | 0.001422271 | mol |
| Constant-pressure reaction heat after10 s | -28.44543 | J |
| Initial excess Gibbs energy | 10.30969 | J |
| Excess Gibbs energy after10 s | 1.291404 | J |
| Gibbs decrease through10 s | 9.018288 | J |
| Two-electron charge ceiling from B after10 s | 274.4566 | C |
Equilibrium fixes a finite endpoint while rate coefficients set approach time; heat, charge and maximum work are different accounts.
The Gibbs decrease is a maximum reversible non-expansion-work bound between the same states under isothermal/isobaric conditions, not work actually harvested by this freely relaxing kinetic path. The kinetic trajectory specifies no electrical device. Do not add reaction heat and Gibbs decrease as independent energy sources or multiply a changing instantaneous reaction Gibbs energy by the entire extent. The charge ceiling assumes quantitative two-electron recovery and supplies neither potential nor current efficiency.
Equilibrium fixes a finite endpoint while rate coefficients set approach time; heat, charge and maximum work are different accounts.
The Gibbs decrease is a maximum reversible non-expansion-work bound between the same states under isothermal/isobaric conditions, not work actually harvested by this freely relaxing kinetic path. The kinetic trajectory specifies no electrical device. Do not add reaction heat and Gibbs decrease as independent energy sources or multiply a changing instantaneous reaction Gibbs energy by the entire extent. The charge ceiling assumes quantitative two-electron recovery and supplies neither potential nor current efficiency.
Captures preserve recipes and replay their calculated results. They are synthetic model evidence, not physical measurements.
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Public practice checks a specific claim. It does not establish independent mastery.
Why is the reversible work bound neither actual output from the kinetic path nor an extra energy source to add to reaction heat?
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