Read this slide. Open the Week 5 worksheet, page 1. Keep it beside the video. This lesson replaces the class on 6 November. We return to the classroom on 13 November.
| Week 4 process | What controls equilibrium? |
|---|---|
| Bulk sublimation | A separate pure solid can coexist with its gas. While solid remains, P_A=P_{\mathrm{sub}}(T) in this model. |
| Surface adsorption | Molecules occupy an adsorbent surface. An isotherm gives uptake q(P_A) per mass of adsorbent. |
Both calculations also need an inventory balance. These conditions answer different questions.
Pause for 4 minutes. Worksheet p. 1, R1. Calculate first. Check your answer on slide 4. If stuck, mark the step and continue.
T=300 K, V=1 L, P_{\mathrm{sub}}=10 kPa. Total volatile amount: n_A=0.002 mol.
n_{\mathrm{cap}}=\frac{P_{\mathrm{sub}}V}{RT},\qquad P_A=\frac{n_{A,\mathrm{gas}}RT}{V}
Use R=8.314462618 kPa L mol^{-1} K^{-1}. State which pressure changes.
Pause for 4 minutes. Worksheet p. 1, R2. Substitute the proposed pressure into both equations. Slide 4 gives the check.
A candidate Langmuir state has P_A=10 kPa, T=300 K, V_g=1 L and m_s=0.010 kg. Given q_s=2 mol/kg, b=0.1 kPa^{-1} and total feed 0.010 mol:
n_{\mathrm{gas}}=\frac{P_AV_g}{RT},\qquad n_{\mathrm{ads}}=m_s\frac{q_s bP_A}{1+bP_A}
Calculate each amount independently. Does their sum equal the stated feed?
A number obtained by subtracting gas moles from the feed still needs to satisfy the isotherm.
Check R1-R2 on worksheet p. 1. Keep your first attempt and write corrections beside it. No extra Lab run is required for this review.
R1: n_{\mathrm{cap}}=0.004009 mol exceeds the available 0.002 mol. No solid remains. P_A=4.989 kPa. Adding the inert gas gives P_{\mathrm{total}}=9.977 kPa while P_A stays unchanged.
R2: At the proposed 10 kPa, n_{\mathrm{gas}}=0.004009 mol and n_{\mathrm{ads}}=0.010000 mol. Their sum, 0.014009 mol, exceeds the feed.
The checked equilibrium is P_A=6.080 kPa, with 0.002438+0.007562=0.010000 mol.
Next: chemical equilibrium also combines an equilibrium relation with conserved amounts.
Read the route on worksheet p. 1. Use the indicated worksheet section at every pause. Open the Lab guide only for the Lab 12 steps.
| Required work | Planned time |
|---|---|
| Video explanations and demonstrations | About 42 min |
| Worksheet, Lab 12, exit ticket and feedback | 128 min |
| Break | 10 min |
There is no required preclass reading or follow-up assignment. Additional models are optional references.
At a pause limit, record the unresolved step and continue. Bring it to class on 13 November. The time budget is a guide, not a speed test.
Read with worksheet p. 2, A1. Use the same synthetic reaction throughout this lesson. You will complete A1-A3 at slide 8.
\mathrm{A_2(g)}\rightleftharpoons 2\mathrm{A(g)}
Initially: 1 mol of A_2, no A and no inert gas. A is a formal teaching species.
n_{A_2}=1\ \mathrm{mol}-\xi,\qquad n_A=2\xi,\qquad 0\leq\xi\leq1\ \mathrm{mol}
Define the dimensionless fraction f=\xi/(1\ \mathrm{mol}). Then n_{\mathrm{total}}=(1+f) mol.
The conserved atom amount is 2n_{A_2}+n_A=2 mol of A atoms.
Read with worksheet p. 2, A2. The Lab 12 extent calculation assumes one ideal gas phase at fixed temperature and total pressure.
For each gas, a_i=y_iP/p^\circ, with p^\circ=100 kPa.
Q=\frac{a_A^2}{a_{A_2}}=\frac{y_A^2}{y_{A_2}}\frac{P}{p^\circ}
Use dimensionless P/p^\circ, not a pressure carrying units inside a logarithm.
Pause for 10 minutes. Worksheet p. 2, A1-A3. Work through the mole table and quotient. Then continue to slide 9.
Check the atom balance at f=0.50.
For finite \ln Q, work inside 0<f<1. The pure-feed and complete-conversion endpoints need limiting interpretations.
Check A1-A3 on worksheet p. 2. Correct the algebra before using it in the following calculations.
y_{A_2}=\frac{1-f}{1+f},\qquad y_A=\frac{2f}{1+f}
Q=\frac{4f^2}{1-f^2}\frac{P}{p^\circ}
At f=0.50: n_{A_2}=0.50 mol, n_A=1.00 mol, y_A=2/3 and y_{A_2}=1/3.
Q=1.3333 at P/p^\circ=1 and Q=5.3333 at P/p^\circ=4.
The atom check is 2(0.50)+1.00=2.00 mol of A atoms. These are specified trial states, not yet equilibrium solutions.
Pause for 6 minutes. Worksheet p. 2, B1. Calculate the driving force at each trial Q, then predict forward or reverse reaction. Check on slide 14.
At 350 K, the supplied standard reaction Gibbs energy is \Delta_rG^\circ=-4000 J/mol of reaction.
\Delta_rG=\Delta_rG^\circ+RT\ln Q
Evaluate Q=1 and Q=10, using R=8.314462618 J mol^{-1} K^{-1}.
Negative \Delta_rG favors increasing extent. Positive \Delta_rG favors decreasing extent. An interior equilibrium has \Delta_rG=0.
Read with worksheet p. 3, B2. Write the substitution now. Complete the numeric comparison at slide 13.
\ln K=-\frac{\Delta_rG^\circ}{RT}
At 350 K, use \Delta_rG^\circ=-4.000 kJ per mol of the reaction as written.
Convert kJ to J before using R=8.314462618 J mol^{-1} K^{-1}.
Calculate \ln K first, then K=\exp(\ln K). A standard Gibbs energy supplied at one temperature is a point value.
Read with worksheet p. 3, B3. Keep the same reaction, temperature and standard states as Route 1.
At the reference temperature 350 K, the synthetic definitions are:
\Delta_rH^\circ=50000\ \mathrm{J/mol},\qquad \Delta_rS^\circ=\frac{54000}{350}\ \mathrm{J\,mol^{-1}K^{-1}}
\Delta_rG^\circ=\Delta_rH^\circ-T\Delta_rS^\circ
Then use the same \ln K=-\Delta_rG^\circ/(RT) relation.
An endothermic reaction can have K>1: the entropy term also contributes to the standard Gibbs energy.
Pause for 10 minutes. Worksheet p. 3, B2-B4. Calculate both routes before opening the worked solutions. Continue to slide 14 for the check.
| Route | Calculate |
|---|---|
| Direct standard Gibbs energy | \ln K and K at 350 K |
| Standard enthalpy and entropy | \Delta_rG^\circ, \ln K and K at 350 K |
Explain why agreement is expected for these mutually consistent synthetic inputs.
Does agreement between two calculations using those definitions independently validate a real chemical system?
Check B1-B4. Mark the energy units and the sign in your worksheet. Retain these values for the remaining cases.
\Delta_rG^\circ=50000-350\left(\frac{54000}{350}\right)=-4000\ \mathrm{J/mol}
\ln K=1.3745412,\qquad K=3.9532626
B1: Q=1 gives \Delta_rG=-4.000 kJ/mol, so forward reaction is favored. Q=10 gives \Delta_rG=+2.7007 kJ/mol, so reverse reaction is favored.
Agreement checks consistent use of the supplied definitions. Real-system prediction still needs valid property data and an appropriate model.
Pause for 15 minutes. Worksheet p. 3, C1-C3. Solve the reference case by hand before checking slide 16.
At 350 K, K=3.9532626, P=100 kPa and p^\circ=100 kPa:
K=\frac{4f^2}{1-f^2}\frac{P}{p^\circ}
Use f=\xi/(1\ \mathrm{mol}), so the mole and dimensionless quantities remain distinct.
Check C1-C3 on worksheet p. 3. Use unrounded values for a tight numerical check.
f=\sqrt{\frac{K}{K+4P/p^\circ}}=0.7050261,\qquad\xi=0.7050261\ \mathrm{mol}
| Quantity | Reference equilibrium |
|---|---|
| n_{A_2} / mol | 0.2949739 |
| n_A / mol | 1.4100521 |
| y_{A_2}, y_A | 0.1730026, 0.8269974 |
Q=3.9532626=K and 2n_{A_2}+n_A=2.0000000 mol of A atoms.
Pause for 8 minutes. Worksheet p. 4, C4. Predict the direction first, then calculate. Check on slide 18.
Keep 350 K, the reaction, initial inventory and p^\circ=100 kPa. Raise the actual total pressure from 100 to 400 kPa.
This is a fixed-T,P reaction calculation. Do not replace it with the fixed-volume inert-gas argument from Week 4.
Check C4 on worksheet p. 4. Compare the same quantities in both cases.
| At 350 K | 100 kPa | 400 kPa |
|---|---|---|
| Standard K | 3.953263 | 3.953263 |
| \xi / mol | 0.705026 | 0.445114 |
| y_A | 0.826997 | 0.616026 |
| y_{A_2} | 0.173003 | 0.383974 |
At a fixed trial composition, raising pressure increases Q because \Delta\nu=+1. Equilibrium shifts toward smaller extent until Q=K again.
Pause for 5 minutes. Worksheet p. 4, D1; Lab guide p. 1. Open Lab 12, select Reset synthetic example, and inspect the listed controls. Then watch slide 20.
Set T=T_{\mathrm{ref}}=350 K, P=p^\circ=100 kPa and inert gas =0 mol.
Change the default \Delta_rC_p^\circ from 30 to 0 J mol^{-1} K^{-1}. Keep the supplied \Delta_rG^\circ, \Delta_rH^\circ, \Delta_rS^\circ and reference \ln K.
For K source for extent and driving force, choose Direct \Delta_rG^\circ at its supplied T. Verify the reaction table starts with 1 mol A_2 and 0 mol A.
Watch the actual Lab demonstration. Follow guide p. 1. Observe the result before beginning D2-D4 on slide 21.
The separate Observed activities panel uses supplied trial values y_{A_2}=0.2, y_A=0.8. It does not automatically show the extent solver’s equilibrium composition.
Pause for 22 minutes. Worksheet p. 4, D2-D4; guide p. 1. Run the cases yourself. Slide 22 provides the pressure demonstration and check.
Identify both axes and the minimum in the reaction Gibbs-energy graph. If blocked, record the control or message and continue at the time limit.
Watch the 400 kPa check and compare D2-D4. Correct your own records. The worked solutions contain the same reference numbers.
The graph plots reaction extent \xi in mol against relative total Gibbs energy [G(\xi)-G(0)]/(RT) in mol.
The selected equilibrium is the minimum within this admitted single neutral ideal-gas reaction model. At the solution, \ln Q-\ln K\approx0 and the atom balance closes.
At 400 kPa, K remains 3.953263 while \xi decreases to 0.445114 mol. A successful calculation checks this model; it does not establish real-gas accuracy or rule out other phases.
Pause for 10 minutes. Save your worksheet and the two exported studies. Resume at slide 24.
Your first comparison changed pressure at fixed temperature.
After the break, change temperature at fixed pressure and ask why K now changes.
You do not need to complete optional reading during the break.
Read with worksheet p. 5, E1. Keep P=p^\circ=100 kPa for the next case.
The direct value \Delta_rG^\circ=-4.000 kJ/mol was supplied at 350 K. It does not describe every temperature.
For this lesson, define a constant reaction enthalpy of +50.000 kJ/mol over 350-400 K, equivalent here to \Delta_rC_p^\circ=0.
The positive enthalpy predicts that increasing temperature increases K for the reaction as written.
Read with worksheet p. 5, E1-E2. Use the reference constant calculated earlier and the stated constant-enthalpy assumption.
\ln\!\left[\frac{K(T)}{K(350)}\right]=\frac{\Delta_rH^\circ}{R}\left(\frac{1}{350}-\frac{1}{T}\right)
For T=400 K, \Delta_rH^\circ=50000 J/mol and \ln K(350)=1.3745412.
First calculate the increment in \ln K, then add it to \ln K(350). Exponentiate once at the end.
This temperature law needs a valid approximation over the interval, consistent reference data and no intervening phase transition.
Pause for 15 minutes. Worksheet p. 5, E1-E3. Calculate before watching slide 27.
Keep pressure, initial inventory and standard states fixed during this temperature comparison.
Check E1-E3 on worksheet p. 5. Compare logarithms before comparing rounded K values.
\ln K(400)=1.3745412+2.1477206=3.5222618
K(400)=33.8609295,\qquad\Delta_rG^\circ(400)=-11.714286\ \mathrm{kJ/mol}
At 100 kPa: \xi=0.945701 mol, y_A=0.972093 and y_{A_2}=0.027907.
The initial atom inventory stays fixed while temperature changes the standard equilibrium constant and the equilibrium composition.
Read with worksheet p. 5, F1 and guide p. 2. Identify the applicable K source before changing the evaluation temperature.
At 400 K, choose van ’t Hoff · constant \Delta H^\circ for the extent solver. Retain T_{\mathrm{ref}}=350 K, the reference \ln K and \Delta_rC_p^\circ=0.
Direct and formation Gibbs-energy inputs supplied at 350 K become unavailable at 400 K. Changing their temperature labels would claim new property data; it would not calculate them.
Custom species, nonzero heat capacities and more detailed temperature models are optional references, outside this lesson’s required work.
Pause for 19 minutes. Worksheet p. 5, F1-F3; guide p. 2. Run the new case and verify a restored file before the demonstration on slide 30.
If a value is unavailable, record the reason. Do not replace it with zero. Record unresolved steps and continue when the pause budget ends.
Watch the 400 K calculation and JSON restore. Check F1-F3 and your three saved records. Worksheet p. 6 lists what to retain.
| Case | T / K | P / kPa | K | \xi / mol |
|---|---|---|---|---|
| 12A | 350 | 100 | 3.953263 | 0.705026 |
| 12B | 350 | 400 | 3.953263 | 0.445114 |
| 12C | 400 | 100 | 33.860929 | 0.945701 |
12A to 12B isolates pressure. 12A to 12C isolates temperature under the specified constant-enthalpy model.
A restored study must reproduce its settings and fresh calculation. Exporting a JSON file does not submit it to the instructor.
Read worksheet p. 6, G. Prepare one concise explanation and one unresolved step, if any. We will discuss these in class on 13 November.
Keep one worksheet and three exported studies. Optional material is not a requirement for completion.
Optional definitions: IUPAC standard equilibrium constant · IUPAC equilibrium constant.
Pause for 10 minutes. Worksheet p. 6, G. Open the Session 5 exit ticket and feedback form. Submit once and wait for Response received.
In your explanation, distinguish K from Q and explain the pressure comparison. Give one numerical result or independent check, with settings and units.
In feedback, report actual study minutes, whether the pace was suitable and the exact step you want explained in class. English or Thai is welcome in the form.
The form is anonymous and does not identify individual attendance. Save your worksheet, corrections and JSON files. Your required Week 5 work ends here.