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=FΔx ; for P–V work under constant P<em>ext, w=−P</em>extΔV (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=McsΔT (Eq 12.2).
- Historical 1 cal = 4.184 J.
- Internal Energy (U): total microscopic E (molecular KE + PE + chemical). State function.
- First Law: ΔU=q+w(system) (Eq 12.3).
- Energy conserved: ΔUuniv=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=CΔT.
- Molar/specific capacities; two varieties:
- C<em>V (constant V) & C</em>P (constant P); C<em>P>C</em>V for gases.
- Coffee-cup calorimeter example (Fe in water) illustrates energy balance.
- Bomb calorimetry: constant V combustion → ΔU=qV.
- Enthalpy H=U+PV (Eq 12.7a).
- At constant P with only P–V work: ΔH=qP (Eq 12.7b).
- Links: ΔH=ΔU+PΔV.
12.4 First Law in Ideal-Gas Processes
- For ideal gases U,H depend only on T.
- Heat capacities (kinetic-theory):
- Monatomic: c<em>V=23R (Eq 12.8); c</em>P=25R.
- General: c<em>P=c</em>V+R (Eq 12.9).
- ΔU=nc<em>VΔT (Eq 12.10); ΔH=nc</em>PΔT (Eq 12.11).
- Path-dependence illustrated (Fig 12.10): two routes ACB & ADB yield same ΔU (1520 J) but different q, w values.
12.5 Molecular Contributions to U & Heat Capacity
- Degrees of freedom (f) & equipartition: each quadratic term contributes 21RT 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 cP.
- Diatomics reach translational + rotational ((7/2)R) at room T; vibrational modes activate at high T (Fig 12.12).
- Solids: Dulong–Petit cV≈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 ΔHf°: enthalpy to form 1 mol compound from elements in std states.
- Reaction enthalpy: ΔH°=∑n<em>iΔH</em>f,i°(products)−∑n<em>jΔH</em>f,j°(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)
- ΔU=ΔH=0.
- w=−nRTlnV</em>1V<em>2=nRTlnP</em>2P<em>1.
- q=−w to keep T constant (Example 12.10).
- Adiabatic (q=0)
- ncVdT=−PdV.
- Relations (γ=cP/cV): TVγ−1=const;PVγ=const (Eqs 12.17–12.18).
- Work equals change in U: w=nc<em>V(T</em>2−T<em>1); enthalpy via nc</em>PΔT.
- 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)=Ce−ε<em>n/k</em>BT (Eq 12.19).
- For harmonic oscillator (vibration): εn=(n+21)hν.
- Relative population: P(0)P(n)=e−nhν/kBT (Eq 12.22).
- CO example: hν=4.52×10−20J; 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:
- Heating liquid from 25→65 °C using q=ncPΔT.
- Vaporization at 65 °C using ΔHvap.
- Combustion enthalpy via bond energies then refined with standard ΔH°₍rxn₎ (–676 kJ·mol⁻¹).
- Energy for 1 kg CH₃OH(g) ≈ −2.1×10⁴ kJ.
- Compute P–V work in engine cylinder (20.6 L atm ≈ –261 J).
- Demonstrates linking calorimetry, phase change, combustion and mechanical work.