Chapter 12 – Thermodynamic Processes & Thermochemistry

Overview of Thermodynamics and Its Relevance

  • Thermodynamics: macroscopic, operational science predicting feasibility, direction & quantitative details of physical/chemical processes.
  • Laws derived empirically; universal validity from black-holes to cells.
  • Independent of atomic theory (would survive its demise) but limited: cannot predict rates or precise property values; needs complementary kinetics/stat-mech.
  • Practical value: prevents wasting resources on impossible conditions; guides optimisation.

12.1 Systems, States & Processes

  • System: portion of universe chosen for study.
    • Closed → no matter exchange ; Open → matter exchange ; Isolated → no matter/energy.
    • Rigid vs non-rigid walls (mechanical); Adiabatic vs diathermal walls (thermal).
  • Surroundings: everything exchanging matter/energy with system.
  • Thermodynamic universe = system + surroundings (isolated overall).
  • Extensive vs Intensive:
    • Extensive add on division (V, m, U).
    • Intensive unchanged on division (T, P).
  • Thermodynamic state: macroscopic condition where properties fixed & time-independent.
    • Defined by constraints; equilibrium when disturbances cease.
    • For 1 mol ideal gas: state fixed by any 2 independent variables (e.g., P & T). PV=nRT gives full surface (Fig 12.1).
  • Processes
    • Change of state; physical or chemical.
    • Reversible: passes through continuous sequence of equilibrium states; infinitesimally slow; path can be reversed by infinitesimal change.
    • Irreversible: real; intermediate states non-equilibrium; cannot map on P-V-T surface.
    • State functions (U, V, T, H …) depend only on initial & final states; Δ independent of path.

12.2 First Law – Internal Energy, Work & Heat

  • Work (w): w=F\Delta x ; for P–V work under constant P{ext}, w=-P{ext}\,\Delta V (Eq 12.1). Sign convention: work done on system positive.
  • Heat (q): energy transfer due to T difference. Measured via calorimetry.
    • Ice calorimeter (volume contraction as ice melts).
    • Relation: q = M c_s \Delta T (Eq 12.2).
    • Historical 1 cal = 4.184 J.
  • Internal Energy (U): total microscopic E (molecular KE + PE + chemical). State function.
  • First Law: \Delta U = q + w \quad (\text{system}) (Eq 12.3).
    • Energy conserved: \Delta U_{univ}=0 (Eq 12.4).
  • Process examples:
    • Expansion of gas against 1 atm (Example 12.1) → system does work, U decreases.
    • Joule paddle experiment illustrates equivalence of work & heat.

12.3 Heat Capacity, Calorimetry & Enthalpy

  • Heat capacity (C): heat required for 1 K rise. q=C\,\Delta T.
  • Molar/specific capacities; two varieties:
    • CV (constant V) & CP (constant P); CP>CV for gases.
  • Coffee-cup calorimeter example (Fe in water) illustrates energy balance.
  • Bomb calorimetry: constant V combustion → \Delta U=q_V.
  • Enthalpy H=U+PV (Eq 12.7a).
    • At constant P with only P–V work: \Delta H = q_P (Eq 12.7b).
    • Links: \Delta H = \Delta U + P\Delta V.

12.4 First Law in Ideal-Gas Processes

  • For ideal gases U, H depend only on T.
  • Heat capacities (kinetic-theory):
    • Monatomic: cV = \frac{3}{2}R (Eq 12.8); cP = \frac{5}{2}R.
    • General: cP = cV + R (Eq 12.9).
    • \Delta U = n cV \Delta T (Eq 12.10); \Delta H = n cP \Delta T (Eq 12.11).
  • Path-dependence illustrated (Fig 12.10): two routes ACB & ADB yield same \Delta U (1520 J) but different q, w values.

12.5 Molecular Contributions to U & Heat Capacity

  • Degrees of freedom (f) & equipartition: each quadratic term contributes \frac{1}{2}RT per mol to U.
    • Translational: 3.
    • Rotational: 2 (linear) or 3 (non-linear).
    • Vibrational: each mode contributes both KE & PE → RT(per mode).
  • Tables 12.2-12.3 compare predicted vs experimental c_P.
    • Diatomics reach translational + rotational ((7/2)R) at room T; vibrational modes activate at high T (Fig 12.12).
  • Solids: Dulong–Petit c_V≈3R at high T; quantum models (Einstein, Debye) explain low-T drop (Fig 12.13).

12.6 Thermochemistry

  • Reaction enthalpy (ΔH): heat at const P for stoichiometric equation.
    • Exothermic ΔH<0 (e.g., thermite; Fig 12.14).
    • Endothermic ΔH>0 (Ba(OH)₂·8H₂O + NH₄NO₃; Fig 12.15).
  • Hess’s Law: reaction ΔH found by algebraic addition of steps; because H is state function.
  • Phase enthalpies: fusion ΔHfus, vaporization ΔHvap (Table 12.4).
  • Standard state (°)
    • 1 atm, specified T (usually 298.15 K), pure phase or 1 m solution.
    • Elements in most stable form assigned H^{°}=0 (except P white).
  • Standard enthalpy of formation \Delta H_f^{°}: enthalpy to form 1 mol compound from elements in std states.
    • Reaction enthalpy: \Delta H^{°} = \sum ni\,\Delta H{f,i}^{°}(\text{products}) - \sum nj\,\Delta H{f,j}^{°}(\text{reactants}) (Eq 12.12).
  • Bond enthalpies (Table 12.5): average gas-phase values enable estimation of (\Delta H_f^{°}) when tabulated data absent (Example 12.9).

12.7 Reversible Ideal-Gas Paths

  • Isothermal (T const)
    • \Delta U = \Delta H =0.
    • w = -nRT\ln\frac{V2}{V1} = nRT\ln\frac{P1}{P2}.
    • q = -w to keep T constant (Example 12.10).
  • Adiabatic (q=0)
    • nc_V dT = -P\,dV.
    • Relations (γ=cP/cV): T V^{\gamma-1}=\text{const};\; P V^{\gamma}=\text{const} (Eqs 12.17–12.18).
    • Work equals change in U: w = n cV (T2-T1); enthalpy via n cP\Delta T.
    • Expansion cools gas (Example 12.11); adiabatic curve steeper than isotherm (Fig 12.20).

12.8 Distribution of Energy Among Molecules (Boltzmann)

  • Probability of molecule in state n: P(n)=C\,e^{-\varepsilonn/kB T} (Eq 12.19).
  • For harmonic oscillator (vibration): \varepsilon_n = (n+\frac12)h\nu.
    • Relative population: \frac{P(n)}{P(0)} = e^{-n h \nu /k_B T} (Eq 12.22).
  • CO example: h\nu=4.52\times10^{-20}\,\text{J}; at 300 K only 3×10⁻⁵ of molecules in v=1.
  • Br₂ example (Example 12.12): lower force constant → much smaller hν, so significant vibrational population even at 300 K (Fig 12.21).

Cumulative Exercise Highlight: Methanol as Gasoline Substitute

  • Steps to evaluate thermal requirements & energy output:
    1. Heating liquid from 25→65 °C using q= n c_P \Delta T.
    2. Vaporization at 65 °C using \Delta H_{vap}.
    3. Combustion enthalpy via bond energies then refined with standard ΔH°₍rxn₎ (–676 kJ·mol⁻¹).
    4. Energy for 1 kg CH₃OH(g) ≈ −2.1×10⁴ kJ.
    5. Compute P–V work in engine cylinder (20.6 L atm ≈ –261 J).
  • Demonstrates linking calorimetry, phase change, combustion and mechanical work.