Advanced Thermodynamics   Final

(Open handouts & note sheet)

  1. Since you don't have STANJAN at your desks this evening, we'll have to assume that

    CH4(g) + 4 NO(g)  arrow right CO2(g) + 2 N2(g) + 2 H2O(g)

    really represents all the important species in that explosion. (It doesn't.) And the table below should give us all the data we need to estimate the stoichiometric explosion overpressure (i.e., how much in excess of 1 atm does the adiabatic explosion generate?).

    SpeciesCH4(g)NO(g)CO2(g)N2(g)H2O(g)
    CP, J/mol K35.3129.8437.129.1233.58
     Delta Hf°, kJ/mol -74.8190.25-393.50.00-241.82

    Remember that explosions occur at fixed volume (so fast that products have not yet expanded). Since this is an estimate, we'll presume all gases are ideal and (foolish us) that CP doesn't change with T.

A two-step problem. Find Texpl and calculate Pexpl from Charles' Law (ideal gas). The overpressure is one atm less than Pexpl. (OK...it's not Charles' Law as such since that relates volume changes with temperature at fixed pressure. We want pressure changes with temperature at fixed volume. Boyle helps us out too. So we'll use P/T fixed at fixed V and n from the Ideal Gas law.)

 Delta Texpl = -  Delta expl /  Summation vCV(products only), but that's not what we have from the tables. So we have to convert H to E and CP to CV. Fortunately, everything being an ideal gas, CV = CP - R. (Where R=8.314 J/mol K.)

It's a little trickier with E, but since H°=E°+P°V,  Delta H°= Delta E°+ Delta (P°V). And as everything is an ideal gas, P°V=nRT°,  Delta H°= Delta E°+RT° Delta n. Aha!  Delta n=0. (5 moles in; 5 moles out.) So  Delta E°= Delta H°!

Life is good. Especially at °.

 Delta E° =  Delta H° = (-393.5) + 2(0) + 2(-241.82) - (-74.81) - 4(90.25) = - 1163.3 kJ/mol as written.

 Summation vCV(products only) =
(37.1-8.314) + 2(29.12-8.314) + 2(33.58-8.314) = 120.9 J/mol K = 0.1209 kJ/mol K. Although we have CP for reactants, they aren't present after the stoichiometric combustion, so they don't soak up  Delta E°.

Therefore,  Delta Texpl = 1163.3 kJ/mol / 0.1209 kJ/mol K = 9620 K.

Texpl =  Delta T+T0 = 9620 + 298 = 9918 K

By our modified Charles' Law,
Pfinal=Pinitial(Tfinal/Tinitial), and Pexpl = 1 atm (9918 K/298 K) = 33.3 atm.
So the overpressure is 32.3 atm. STANJAN would find it to be much less.

BET diagram
  • On the right is Shaw's Fig. 5.13. It is a BET plot for the adsorption of N2 on porous silica gel at 77 K.

    Given that N2 molecules occupy a surface area of 16.2×10-20 m² each at this temperature, estimate the surface area per gram of this sample.

    Note that the ordinate values have been multiplied by 1,000 to give the labelled values (thus the "103") and the volumes have already been scaled on a per gram basis. Remember that "stp" means 1 atm and 273 K not 298 K.

    Given the size of the graph, let's just pretend that it goes through the origin, i.e., the intercept is zero. We'll incur only a trivial error thereby.

  • By BET, p/[V(p0-p)] is supposed to be linear in p/p0, and from the figure, it seems to be so up to about p/p0~0.27. Also Vmono is estimated as 1/[slope+intercept], but if yintercept~0 (to my old eyeballs anyway...well, yes, the line hits the y-axis just a tad above 0; I'm unconcerned.), Vmono~1/slope.

    So if the intercept is close enough to zero, the slope is any y on the line divided by its x. Your choice actually. Mine is (0.16,0.001) or slope = 0.00625 g sample per cc N2 at STP. Or Vmono=1/0.00625=160 cc N2 @ STP per gram sample.

    Now all we need to know is how much area 160 cc of N2 occupies when it adsorbs. That we can get from the 16.2×10-20 m² per molecule by determining the number of molecules in 160 cc of gas at STP. Assume an ideal gas, then n=PV/RT or
    n = 1 atm × 0.160 L / (0.08206 L atm/mol K × 273 K) = 0.0071 moles
    N = n NAv = 0.0071 × 6.022×1023 = 4.3×1021 molecules.
    Amono = 16.2×10-20 m²/molecule × 4.3×1021 molecules = 700 m² / g sample

  • All microstates are equally likely. Knowing that, determine the ratio of B to A versions of a system at a fixed energy from the following information: Version A consists of 3 oscillators and 4 quanta, but due to structural differences, B consists of 4 oscillators and only 3 quanta. (Clearly B's quanta are 4/3 the size of A's, but that's of no consequence here. All that matters here is that for A, N=3 and Q=4, but for B, N=4 and Q=3.)
  • Yes, this is the giveaway question.

    Since all microstates are equally likely, the chances of seeing the system as B vs. A is just the ratio of the microstates available to those two, viz., WB/WA.

    So we must either remember that for the easy case of the harmonic oscillator,
    W = (Q+N-1)!/[Q!(N-1)!],
    or we have to draw out the energy levels and populate the legitimate configurations and add up their weights.

    I choose the formula. :)

    Since Q+N-1 is the same for both A and B, the ratio becomes even simpler:

    [B]/[A] = [QA!(NA-1)!] / [QB!(NB-1)!] = [4!2!]/[3!3!] = 1.33

    And indeed any [(n+1)!(n-1)!] is > [n!n!] means that oscillators are worth more than quanta in creating microstates. Interesting.

  • Problem #3 determined a fixed energy equilibrium constant for a microscopic system. But we're more familiar with a fixed temperature KP for a macroscopic (~NAv) system. Let's estimate that to one significant figure from statistical mechanics for the reaction:

    79Br2(g) + 12C81Br4(g)  arrow right 79Br81Br(g) + 79Br12C81Br3(g)

    We can't really assume a temperature such that vibrations are inactive (vBr2 = 323 cm-1 !), but we do know that they'll all be almost the same for either substituted version of each molecule. And T needn't be above carbon tetrabromide's boiling point since CBr4 has quite a reasonable vapor pressure. So let's say T=298 K. (Why am I so cavalier about that?)

  • I'm so cavalier because it is not going to make much difference WHAT temperature I pick! That's because (a)  Delta n=0 and (b) 79~81 or rather their ratio 81/79=1.025 is so very close to 1. The T dependence of KTRANS disappears since  Delta n=0. The T dependence of KROT disappears since we have equal numbers of diatoms and 3-d polyatoms in reactants and products. The T dependence in KVIB probably doesn't disappear, but ratios of frequencies, v, will depend on the SQUARE ROOTS of ratios of masses which will be 1.025&3178;~1.013, and even more negligible ratio! So stuff will cancel left and right (and up and down).

    Even the big term e Delta D0/RT, will be uninteresting since  Delta D0 depends on those same small differences in the zero-point energies of much too similar bromine isotopes.

    So what's left?

    Electronic? Not on a bet! Different isotopes have the same electronic structure.

    Rotational symmetries? BINGO. While there'll be no T dependence in KROT, that doesn't mean KROT itself vanishes to 1. It is true that the moments of inertia change by some really trivial amount on substitution of 79 for 81 and vice versa, but we're looking for a first significant figure effect. And that's symmetry factors,  sigma .

    KROT = [ sigma 79Br2  sigma C81Br4] / [ sigma 79Br81Br  sigma 79BrC81Br3] = [ 2 × 12 ] / [ 1 × 3 ] = 8

    where we've recognized that zROT is inversely proportional to  sigma and that 79BrC81Br3 has only the one C3 axis for rotation and the tetrahedral C81Br4 can be oriented by grabbing any one of the 4 Br's then can be rotated about that Br-C axis to any of 3 orientations, 4×3=12. Or we could've gone to the symmetry tables for C3v and Td, respectively.

    So our 1 significant figure guess for K = 8.

  • Below 216.58 K, its triple point, CO2 has no liquid phase and so must sublime to create its vapor pressure. Estimate  Delta Hsubl at 205 K from the data below.

    T (K)194.7205216.58
    PCO2 (atm)1.0002.2425.114
  • Clausius-Clayeron helps us here with

    ln(P2/P1) = - ( Delta Hsubl/R) [(1/T2) - (1/T1)]
    or
     Delta Hsubl = R ln(P2/P1) / [(1/T1) - (1/T2)]

    Now our only question is what to choose for "1" and "2" from among the 3 data points. The value at 205 could be estimated by letting T1=194.7 K and T2=216.58 K. The resulting  Delta Hsubl would be a best estimate for the middle of the range or <T> = ½(194.7+216.58) ~ 206 K, close enough. But we wouldn't know how  Delta Hsubl might have changed over the interval; so we'd have no built-in error estimate.

    Better would be to calculate  Delta Hsubl between the 1st two T's and again between the 2nd two T's and take THAT average. After all, the formula above varies non-linearly in T (and P) but to the extent that CP's don't change very much, we'd expect  Delta Hsubl to vary linearly with T. So

     Delta HA = 8.314 ln(2.242/1.000) / [(1/194.7) - (1/205)] = 26,011 J/mol = 26.01 kJ/mol

     Delta HB = 8.314 ln(5.114/2.224) / [(1/205) - (1/216.58)] = 26,543 J/mol = 26.54 kJ/mol

     Delta Hsubl(205 K) = ½ (26.01+26.54) = 26.28 kJ/mol +/- 0.27 kJ/mol

    Just for jollies:

     Delta HC = 8.314 ln(5.114/1.000) / [(1/194.7) - (1/216.58)] = 26,149 J/mol = 26.15 kJ/mol, not as good as the answer above.

    10 pt. BONUS:CV is often approximated as a+bT+cT2 where a,b,c are experimentally fitted parameters. Use those parameters to find A,B,C where Z~DeAlnT+BT+CT2 and D is just an undetermined constant independent of T.

    CV = [dE/dT]V and E = +kT² [d lnZ / dT]V so

    CV = 2kT [d lnZ / dT]V + kT² [d²lnZ / dT²]V]

    ln Z = ln D + ln eAlnT+BT+CT² = ln D + AlnT + BT + CT²

    [d lnZ / dT]V = A/T + B + 2CT

    [d²lnZ / dT²] = -A/T² + 2C

    Substitute:

    CV = k [ 2A + 2BT + 4CT² ] + k [ -A + 2CT² ]

    CV = k [ A + 2BT + 6CT² ] = a + bT + cT²

    so

    A = a/k, B = b/2k, and C = c/6k.


    Last modified 15 December 1997.