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SCIENCE · INVESTIGATE AND EXPLAIN

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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Try

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 experiment

Predict

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.

Reset keeps your prediction, captures and practice history.

B concentration (mol/L)time (s)0600.044888460
  • 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
B concentration approaching finite equilibrium
time (s)B concentration (mol/L)
00
10.004282316
20.008157116
30.01166318
40.0148356
50.01770612
60.02030348
70.02265366
80.0247802
90.02670437
100.02844543
110.0300208
120.03144626
130.03273607
140.03390314
150.03495914
160.03591466
170.03677924
180.03756155
190.03826941
200.03890991
210.03948946
220.04001386
230.04048835
240.04091769
250.04130618
260.04165769
270.04197575
280.04226355
290.04252396
300.04275958
310.04297279
320.0431657
330.04334026
340.0434982
350.04364112
360.04377043
370.04388744
380.04399332
390.04408911
400.0441758
410.04425423
420.0443252
430.04438941
440.04444752
450.0445001
460.04454767
470.04459071
480.04462966
490.0446649
500.04469679
510.04472565
520.04475175
530.04477538
540.04479675
550.0448161
560.0448336
570.04484943
580.04486376
590.04487672
600.04488846
Calculated under the declared model
QuantityValueUnit
Equilibrium B concentration0.045mol/L
B concentration after10 s0.02844543mol/L
Forward rate coefficient0.075s⁻¹
Reverse rate coefficient0.025s⁻¹
Time to90% of equilibrium B23.02585s
Reaction extent after10 s0.001422271mol
Constant-pressure reaction heat after10 s-28.44543J
Initial excess Gibbs energy10.30969J
Excess Gibbs energy after10 s1.291404J
Gibbs decrease through10 s9.018288J
Two-electron charge ceiling from B after10 s274.4566C

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.

Understand

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.

Reconstruct the evidence

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.

For conserved C=A+B, equilibrium gives B_eq=CK/(1+K). The reversible first-order law dB/dt=kf(C−B)−kr B has solution B=B_eq[1−exp(−(kf+kr)t)] for initially pure A. Rate ratio fixes equilibrium, while the sum fixes relaxation time. The90%-of-equilibrium time is ln10/.100=23.02585 s for every supplied K, but the fraction of initial A converted at that time is .90K/(1+K).

Separate state functions and kinetic paths

For this ideal isothermal/isobaric mixture, Gibbs excess above equilibrium is RT V[A ln(A/A_eq)+B ln(B/B_eq)]. Concentrations and volume use matching mol/L and L units; ratios are dimensionless. At B=0 the limit B ln B is zero, not an error or infinite total energy. Gibbs excess falls along the supplied relaxation. Its decrease bounds reversible non-expansion work between those states; the freely relaxing kinetic path does not itself deliver that bound.

The stipulated constant reaction enthalpy gives constant-pressure reaction heat −20000 V B joules when only pressure-volume work is performed. The Gibbs bound is a different thermodynamic account, not additional energy to add to the heat. An alternative work-producing path would require its own heat/work balance. A hypothetical quantitative two-electron recovery of B gives Q_max=2FVB, not actual usable voltage, current efficiency or a device specification.

Changed case: predict, then check

At C=.040 M and K1, equilibrium B=.020 M; at10 s B=.0126424 M. In .050 L the extent is .000632121 mol, so the heat under the stated no-nonexpansion-work path is−12.6424 J. At90% of the equilibrium amount only45% of initial A has converted. Changing the common rate scale changes the approach time without changing K; adding a catalyst cannot establish a new fixed-temperature equilibrium constant.

Retained investigation

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. Why is the reversible work bound neither actual output from the kinetic path nor an extra energy source to add to reaction heat?

Source and safety boundary

Primary conceptual references checked30 October2026: OpenStax equilibrium calculations, free energy, and potential/free-energy/equilibrium. Original fictional data and analysis; no physical manipulation, actual assay certification or independent learner mastery is asserted. Retain first report, critique, revision and a separately frozen new assignment.

Apply

For K3, reaching90% of equilibrium B converts what fraction of initially pure A?

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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