Distinguish a catalytic time scale from an equilibrium ratio
Dynamic equilibrium has equal opposing rates, not zero molecular transformation.
Learning outcome: Compare multiplier settings from two starting compositions. Verify the common endpoint, matching nonzero equilibrium rates and different approach speeds.
Starting recap
Refresh dimensionless activities, component balances, admissible roots, normalized partial pressures and independent versus shared measurement errors.
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Try
With kf=.40 and kr=.10 s⁻¹, total1 M gives Aeq=.20 M and a relaxation time2 s. Multiplying both constants by3 keeps Aeq but changes the time to2/3 s.
Open the experimentPredict
Would changing only the forward constant represent a catalyst for the same thermodynamic equilibrium?
Experiment
Compare multiplier settings from two starting compositions. Verify the common endpoint, matching nonzero equilibrium rates and different approach speeds.
Change equilibration speed without changing its endpoint
Worked teaching model · synthetic values · Fictional elementary isomer pair A⇌B, total1.00 M, kf=.40s⁻¹ and kr=.10s⁻¹ times the same multiplier. K=kf/kr=4; Aeq=.20 M. This bounded catalytic model changes both rates consistently, not the equilibrium constant or conserved inventory.
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- A: solid
- B: long dashes
Axes rescale. A quotient comparison, inventory intersection and relaxation trajectory have different horizontal meanings; inspect labels rather than treating every curve as elapsed time.
All calculated plot coordinates
| time (s) | concentration (mol/L) |
|---|---|
| 0 | 0.8 |
| 0.1666667 | 0.7520266 |
| 0.3333333 | 0.707889 |
| 0.5 | 0.6672805 |
| 0.6666667 | 0.6299188 |
| 0.8333333 | 0.5955444 |
| 1 | 0.5639184 |
| 1.166667 | 0.5348211 |
| 1.333333 | 0.5080503 |
| 1.5 | 0.4834199 |
| 1.666667 | 0.4607589 |
| 1.833333 | 0.4399098 |
| 2 | 0.4207277 |
| 2.166667 | 0.4030793 |
| 2.333333 | 0.3868419 |
| 2.5 | 0.3719029 |
| 2.666667 | 0.3581583 |
| 2.833333 | 0.3455126 |
| 3 | 0.3338781 |
| 3.166667 | 0.3231738 |
| 3.333333 | 0.3133254 |
| 3.5 | 0.3042644 |
| 3.666667 | 0.2959278 |
| 3.833333 | 0.2882579 |
| 4 | 0.2812012 |
| 4.166667 | 0.2747087 |
| 4.333333 | 0.2687353 |
| 4.5 | 0.2632395 |
| 4.666667 | 0.2581832 |
| 4.833333 | 0.2535311 |
| 5 | 0.249251 |
| 5.166667 | 0.2453131 |
| 5.333333 | 0.2416901 |
| 5.5 | 0.2383567 |
| 5.666667 | 0.2352899 |
| 5.833333 | 0.2324683 |
| 6 | 0.2298722 |
| 6.166667 | 0.2274838 |
| 6.333333 | 0.2252863 |
| 6.5 | 0.2232645 |
| 6.666667 | 0.2214044 |
| 6.833333 | 0.219693 |
| 7 | 0.2181184 |
| 7.166667 | 0.2166698 |
| 7.333333 | 0.2153369 |
| 7.5 | 0.2141106 |
| 7.666667 | 0.2129824 |
| 7.833333 | 0.2119444 |
| 8 | 0.2109894 |
| 8.166667 | 0.2101107 |
| 8.333333 | 0.2093023 |
| 8.5 | 0.2085585 |
| 8.666667 | 0.2078742 |
| 8.833333 | 0.2072446 |
| 9 | 0.2066654 |
| 9.166667 | 0.2061325 |
| 9.333333 | 0.2056421 |
| 9.5 | 0.205191 |
| 9.666667 | 0.204776 |
| 9.833333 | 0.2043941 |
| 10 | 0.2040428 |
| time (s) | concentration (mol/L) |
|---|---|
| 0 | 0.2 |
| 0.1666667 | 0.2479734 |
| 0.3333333 | 0.292111 |
| 0.5 | 0.3327195 |
| 0.6666667 | 0.3700812 |
| 0.8333333 | 0.4044556 |
| 1 | 0.4360816 |
| 1.166667 | 0.4651789 |
| 1.333333 | 0.4919497 |
| 1.5 | 0.5165801 |
| 1.666667 | 0.5392411 |
| 1.833333 | 0.5600902 |
| 2 | 0.5792723 |
| 2.166667 | 0.5969207 |
| 2.333333 | 0.6131581 |
| 2.5 | 0.6280971 |
| 2.666667 | 0.6418417 |
| 2.833333 | 0.6544874 |
| 3 | 0.6661219 |
| 3.166667 | 0.6768262 |
| 3.333333 | 0.6866746 |
| 3.5 | 0.6957356 |
| 3.666667 | 0.7040722 |
| 3.833333 | 0.7117421 |
| 4 | 0.7187988 |
| 4.166667 | 0.7252913 |
| 4.333333 | 0.7312647 |
| 4.5 | 0.7367605 |
| 4.666667 | 0.7418168 |
| 4.833333 | 0.7464689 |
| 5 | 0.750749 |
| 5.166667 | 0.7546869 |
| 5.333333 | 0.7583099 |
| 5.5 | 0.7616433 |
| 5.666667 | 0.7647101 |
| 5.833333 | 0.7675317 |
| 6 | 0.7701278 |
| 6.166667 | 0.7725162 |
| 6.333333 | 0.7747137 |
| 6.5 | 0.7767355 |
| 6.666667 | 0.7785956 |
| 6.833333 | 0.780307 |
| 7 | 0.7818816 |
| 7.166667 | 0.7833302 |
| 7.333333 | 0.7846631 |
| 7.5 | 0.7858894 |
| 7.666667 | 0.7870176 |
| 7.833333 | 0.7880556 |
| 8 | 0.7890106 |
| 8.166667 | 0.7898893 |
| 8.333333 | 0.7906977 |
| 8.5 | 0.7914415 |
| 8.666667 | 0.7921258 |
| 8.833333 | 0.7927554 |
| 9 | 0.7933346 |
| 9.166667 | 0.7938675 |
| 9.333333 | 0.7943579 |
| 9.5 | 0.794809 |
| 9.666667 | 0.795224 |
| 9.833333 | 0.7956059 |
| 10 | 0.7959572 |
| Quantity | Value | Unit |
|---|---|---|
| Equilibrium A | 0.2 | mol/L |
| Equilibrium B | 0.8 | mol/L |
| Relaxation time constant | 2 | s |
| Forward equilibrium rate | 0.08 | mol/(L s) |
| Reverse equilibrium rate | 0.08 | mol/(L s) |
| A after 2 seconds | 0.4207277 | mol/L |
At equilibrium the opposing rates agree; the elementary transformations have not stopped.
Multiplying both rate constants preserves kf/kr while shortening the relaxation time. Changing only the forward rate would change this model equilibrium and would not represent a catalyst for the same thermodynamic reaction. These first-order rates are an explicit mechanism model, not inferred from the net equation alone.
These calculated packets are not performed chemical measurements. Keep feasible inventories, activity conventions, fitting observations and independent checks distinct.
At equilibrium the opposing rates agree; the elementary transformations have not stopped.
Multiplying both rate constants preserves kf/kr while shortening the relaxation time. Changing only the forward rate would change this model equilibrium and would not represent a catalyst for the same thermodynamic reaction. These first-order rates are an explicit mechanism model, not inferred from the net equation alone.
Captures preserve recipes and replay their calculated results. They are synthetic model evidence, not physical measurements.
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Which mechanistic assumption permits using K=kf/kr here, and why is it not automatic for an arbitrary net equation?
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