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SCIENCE · INVESTIGATE AND EXPLAIN

Test an intermediate profile without singular equal-rate arithmetic

The candidate sequence A→B→C forms B in one step and consumes it in the next.

Learning outcome: Compare(.2,.2),(.2,.4) and(.4,.2). Retain A,B,C profiles, the peak time and conserved total; explain how formation and consumption compete at the peak.

Starting recap

Distinguish a net reaction coefficient, empirical exponent and elementary step. Refresh logarithmic ratios, signed residuals, concentration/time dimensions and parameter identifiability.

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Try

For equal constants k=.20 s⁻¹, B=.20t exp(−.20t) reaches its maximum at 5 s, where A=B=exp(−1)≈.367879 and C≈.264241.

Open the experiment

Predict

Does the intermediate peak mean the entire irreversible network has reached chemical equilibrium?

Experiment

Compare(.2,.2),(.2,.4) and(.4,.2). Retain A,B,C profiles, the peak time and conserved total; explain how formation and consumption compete at the peak.

Test an intermediate profile and equal-rate limit

Worked teaching model · synthetic values · Fictional isomers A→B→C, initial A = 1.00 M and B,C = 0; irreversible constant-volume first-order steps. B=k1/(k2−k1)[exp(−k1t)−exp(−k2t)]; equal-rate limit B=kt exp(−kt). Analytical supplied solution, not proof that a real species is an obligatory intermediate.

Reset keeps your prediction, captures and practice history.

concentration (mol/L)time (s)02010
  • A: solid
  • B: long dashes
  • C: short dashes

Axes rescale. A concentration trajectory, initial-rate comparison and inverse-temperature plot have different horizontal meanings; use the labels rather than assuming every curve shows elapsed time.

All calculated plot coordinates
A
time (s)concentration (mol/L)
01
0.20.9607894
0.40.9231163
0.60.8869204
0.80.8521438
10.8187308
1.20.7866279
1.40.7557837
1.60.726149
1.80.6976763
20.67032
2.20.6440364
2.40.6187834
2.60.5945205
2.80.5712091
30.5488116
3.20.5272924
3.40.506617
3.60.4867523
3.80.4676664
40.449329
4.20.4317105
4.40.4147829
4.60.398519
4.80.3828929
50.3678794
5.20.3534547
5.40.3395955
5.60.3262798
5.80.3134862
60.3011942
6.20.2893842
6.40.2780373
6.60.2671353
6.80.2566608
70.246597
7.20.2369278
7.40.2276377
7.60.2187119
7.80.2101361
80.2018965
8.20.19398
8.40.186374
8.60.1790661
8.80.1720449
90.1652989
9.20.1588174
9.40.1525901
9.60.146607
9.80.1408584
100.1353353
10.20.1300287
10.40.1249302
10.60.1200316
10.80.1153251
110.1108032
11.20.1064585
11.40.1022842
11.60.09827359
11.80.09442022
120.09071795
12.20.08716085
12.40.08374323
12.60.08045961
12.80.07730474
130.07427358
13.20.07136127
13.40.06856315
13.60.06587475
13.80.06329177
140.06081006
14.20.05842567
14.40.05613476
14.60.05393369
14.80.05181892
150.04978707
15.20.04783489
15.40.04595926
15.60.04415717
15.80.04242574
160.0407622
16.20.0391639
16.40.03762826
16.60.03615283
16.80.03473526
170.03337327
17.20.03206469
17.40.03080741
17.60.02959944
17.80.02843882
180.02732372
18.20.02625234
18.40.02522297
18.60.02423397
18.80.02328374
190.02237077
19.20.0214936
19.40.02065083
19.60.01984109
19.80.01906311
200.01831564
B
time (s)concentration (mol/L)
00
0.20.03804981
0.40.07239182
0.60.1033005
0.80.1310319
10.1558251
1.20.1779031
1.40.1974738
1.60.2147313
1.80.2298561
20.2430168
2.20.2543702
2.40.2640623
2.60.2722291
2.80.2789971
30.284484
3.20.2887991
3.40.2920441
3.60.2943135
3.80.2956948
40.2962695
4.20.296113
4.40.2952952
4.60.293881
4.80.2919303
50.2894986
5.20.2866372
5.40.2833937
5.60.2798116
5.80.2759316
60.2717906
6.20.2674232
6.40.2628607
6.60.2581321
6.80.2532641
70.2482811
7.20.2432053
7.40.2380572
7.60.2328554
7.80.2276169
80.2223571
8.20.2170902
8.40.2118287
8.60.2065843
8.80.2013672
90.1961868
9.20.1910513
9.40.1859683
9.60.1809444
9.80.1759854
100.1710964
10.20.166282
10.40.1615461
10.60.1568919
10.80.1523225
110.14784
11.20.1434465
11.40.1391435
11.60.1349323
11.80.1308138
120.1267885
12.20.1228567
12.40.1190185
12.60.1152738
12.80.1116223
130.1080633
13.20.1045963
13.40.1012204
13.60.09793458
13.80.09473783
140.09162897
14.20.08860673
14.40.08566976
14.60.08281666
14.80.08004596
150.07735614
15.20.07474566
15.40.07221292
15.60.06975631
15.80.06737419
160.06506491
16.20.06282682
16.40.06065825
16.60.05855754
16.80.05652302
170.05455305
17.20.05264597
17.40.05080016
17.60.04901401
17.80.04728591
180.04561428
18.20.04399758
18.40.04243425
18.60.0409228
18.80.03946174
190.03804961
19.20.03668498
19.40.03536644
19.60.03409262
19.80.03286217
200.03167377
C
time (s)concentration (mol/L)
00
0.20.00116075
0.40.004491834
0.60.009779113
0.80.01682436
10.02544418
1.20.03546907
1.40.04674242
1.60.05911967
1.80.07246753
20.08666313
2.20.1015934
2.40.1171543
2.60.1332504
2.80.1497939
30.1667044
3.20.1839085
3.40.2013389
3.60.2189343
3.80.2366388
40.2544015
4.20.2721765
4.40.2899219
4.60.3076
4.80.3251769
50.342622
5.20.3599081
5.40.3770108
5.60.3939086
5.80.4105823
60.4270151
6.20.4431926
6.40.459102
6.60.4747326
6.80.4900751
70.505122
7.20.519867
7.40.5343052
7.60.5484328
7.80.5622471
80.5757464
8.20.5889298
8.40.6017973
8.60.6143496
8.80.6265879
90.6385144
9.20.6501313
9.40.6614416
9.60.6724486
9.80.6831562
100.6935683
10.20.7036893
10.40.7135237
10.60.7230764
10.80.7323524
110.7413569
11.20.750095
11.40.7585722
11.60.7667941
11.80.774766
120.7824936
12.20.7899825
12.40.7972383
12.60.8042666
12.80.811073
130.8176631
13.20.8240424
13.40.8302165
13.60.8361907
13.80.8419704
140.847561
14.20.8529676
14.40.8581955
14.60.8632497
14.80.8681351
150.8728568
15.20.8774194
15.40.8818278
15.60.8860865
15.80.8902001
160.8941729
16.20.8980093
16.40.9017135
16.60.9052896
16.80.9087417
170.9120737
17.20.9152893
17.40.9183924
17.60.9213866
17.80.9242753
180.927062
18.20.9297501
18.40.9323428
18.60.9348432
18.80.9372545
190.9395796
19.20.9418214
19.40.9439827
19.60.9460663
19.80.9480747
200.9500106
Calculated under the declared model
QuantityValueUnit
A at 5 s0.3678794mol/L
Intermediate B at 5 s0.2894986mol/L
Final C at 5 s0.342622mol/L
Conserved total at 5 s1mol/L
Intermediate maximum time4.054651s

A rising and falling intermediate requires both a formation and a consumption account.

At equal constants use the finite limit B=kt exp(−kt), not division by zero. The intermediate peak occurs when its formation and consumption rates match; it is not chemical equilibrium of the whole irreversible network. A transient detected species is not automatically an obligatory intermediate without discriminating kinetic or structural evidence.

These calculated packets are not performed chemical or instrument measurements. Keep the hypothesis, fitting observations, withheld checks and exposure record distinct.

A rising and falling intermediate requires both a formation and a consumption account.

At equal constants use the finite limit B=kt exp(−kt), not division by zero. The intermediate peak occurs when its formation and consumption rates match; it is not chemical equilibrium of the whole irreversible network. A transient detected species is not automatically an obligatory intermediate without discriminating kinetic or structural evidence.

Captures preserve recipes and replay their calculated results. They are synthetic model evidence, not physical measurements.

Understand

Separate formation and consumption

The candidate sequence A→B→C forms B in one step and consumes it in the next. A rising then falling B profile reflects the competition between those rates. With initial A1 M and no products, the irreversible first-order assumptions determine all three trajectories; an observed transient alone does not establish that every real molecule follows this path.

Use the supplied analytic solution

A=exp(−k1t). For unequal constants, B=k1[exp(−k1t)−exp(−k2t)]/(k2−k1), and C=1−A−B. The numerator and denominator change signs together when the constants swap, preserving nonnegative amounts. The expression is supplied as a solved model; deriving the coupled differential equations is optional deeper work.

Handle equal constants physically

When k1=k2=k, the unequal-rate expression has a zero-over-zero form, not zero concentration or an infinite concentration. Its finite limit is B=kt exp(−kt). At k=.20 and t=5s, A and B both equal exp(−1), while C=1−2exp(−1). All amounts remain finite and sum to1.

Interpret the intermediate maximum

At the B peak, k1A=k2B so its instantaneous formation and consumption rates match. This does not mean the complete irreversible network is at equilibrium: A is still being consumed and C produced. For unequal constants the peak time is ln(k2/k1)/(k2−k1); the equal-rate limit is1/k.

Transfer and propose discriminating evidence

For k1=.10 and k2=.20 s⁻¹, predict peak time ln2/.10≈6.931s. At that time A=.50,B=.25,C=.25 M. Independent identity, calibrated response and perturbation evidence would be needed to establish B as an obligatory intermediate rather than a parallel transient species.

Source and evidence boundary

Conceptual reference checked 30 October 2026: OpenStax Chemistry 2e. All numerical packets, prose and diagrams are original. Models are supplied/simulated, not measured rate constants or observed chemical mechanisms. No reactive substances, heating, optical instrument, catalytic preparation or physical chemical procedure is requested. Retain predictions, contrasting evidence, residuals and a changed-case explanation.

Apply

For equal consecutive first-order constants k, the finite intermediate expression is:

Public practice checks a specific claim. It does not establish independent mastery.

Why would seeing a transient species not by itself prove it is an obligatory intermediate?

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