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Review

1. Checklist of Key Concepts

Section 3.1: Conservation of Energy

  1. First Law of Thermodynamics

    • The internal energy change of a system equals the heat absorbed plus the work done on it:

    ΔU=q+w.\Delta U = q + w.
    • In differential form: dU=δq+δwdU = \delta q + \delta w, or equivalently δq=dU−δw\delta q = dU - \delta w.

  2. State Functions vs. Path Functions

    • UU is a state function: ΔU\Delta U depends only on the initial and final states, and dUdU is an exact differential (∮dU=0\oint dU = 0).

    • qq and ww are path functions: their values depend on the process path, and δq\delta q, δw\delta w are inexact differentials.

  3. Sign Convention (Chemistry Convention)

    • q>0q > 0: heat absorbed by the system.

    • w>0w > 0: work done on the system.

    • For PVPV work: δw=−P dV\delta w = -P\,dV, so compression (dV<0dV < 0) gives w>0w > 0.

  4. Generalized Work

    • Many work modes share a generalized force ×\times generalized displacement structure: PVPV work (−P dV-P\,dV), surface work (γ dA\gamma\,dA), elastic work (k dlk\,dl), electrical work (E dqel\mathcal{E}\,dq_{\mathrm{el}}), and chemical work (μ dN\mu\,dN).

  5. Free Expansion

    • Expansion into vacuum: Pext=0P_{\mathrm{ext}} = 0, so w=0w = 0. If the container is also insulated, q=0q = 0 and ΔU=0\Delta U = 0. For an ideal gas, ΔT=0\Delta T = 0 as well.

    • Free expansion is the extreme case of an irreversible process: the gas changes state while doing no work and exchanging no heat.


Section 3.2: Applications of the First Law

  1. Thermodynamic Processes

    • Quasi-static: carried out infinitesimally slowly; the system remains near equilibrium at all times.

    • Reversible: quasi-static and free of dissipative effects (friction, turbulence, viscous drag, etc.); can be reversed with no net change to system or surroundings.

    • Irreversible: any real process that violates one or more conditions for reversibility.

  2. Reversible Work Bounds

    • For a given expansion (ΔV>0\Delta V > 0), a reversible process does the maximum work on the surroundings (∣wrev∣≥∣wirrev∣|w_{\mathrm{rev}}| \geq |w_{\mathrm{irrev}}|).

    • For a given compression, a reversible process requires the minimum work input.

  3. Five-Step First Law Workflow

    1. Choose two independent variables (e.g., V,TV, T or P,TP, T).

    2. Rewrite the First Law in terms of those variables.

    3. Apply process constraints (isothermal, isochoric, isobaric, adiabatic).

    4. Specify the equation of state (e.g., ideal gas).

    5. Integrate to find qq, ww, ΔU\Delta U.

  4. First Law with VV and TT as Independent Variables

    • General form:

    δq  =  CV dT  +  [(∂U∂V)T+P]dV.\delta q \;=\; C_V \, dT \;+\; \left[\left(\frac{\partial U}{\partial V}\right)_T + P\right] dV.
    • For an ideal gas, (∂U/∂V)T=0(\partial U/\partial V)_T = 0, simplifying to δq=CV dT+P dV\delta q = C_V\,dT + P\,dV.

  5. Common Ideal-Gas Processes

    • Isochoric (dV=0dV = 0): w=0w = 0, q=CV ΔTq = C_V\,\Delta T, ΔU=CV ΔT\Delta U = C_V\,\Delta T.

    • Isothermal (dT=0dT = 0): ΔU=0\Delta U = 0 (ideal gas), q=−w=NkBTln⁡(V2/V1)q = -w = Nk_{\mathrm{B}}T\ln(V_2/V_1).

    • Adiabatic (δq=0\delta q = 0): ΔU=w=CV ΔT\Delta U = w = C_V\,\Delta T, and TVγ−1=constTV^{\gamma - 1} = \text{const} (equivalently PVγ=constPV^\gamma = \text{const}), where γ=CP/CV\gamma = C_P/C_V.

  6. Microscopic Interpretation of the First Law

    • From U=∑ipiEiU = \sum_i p_i E_i:

    dU=∑iEi dpi⏟δq+∑ipi dEi⏟δw.dU = \underbrace{\sum_i E_i\, dp_i}_{\delta q} + \underbrace{\sum_i p_i\, dE_i}_{\delta w}.
    • Heat changes which states are occupied (probabilities shift; energy levels fixed).

    • Work changes the energies of the states (energy levels shift; probabilities fixed).


Section 3.3: Enthalpy

  1. Definition and Motivation

    • Enthalpy: H=U+PVH = U + PV.

    • At constant pressure with PVPV-only work: δqP=dH\delta q_P = dH, so qP=ΔHq_P = \Delta H.

    • Defines a state function that plays the same role at constant PP that UU plays at constant VV.

  2. Heat Capacity at Constant Pressure

    CP=(∂H∂T)P=(∂U∂T)P+P(∂V∂T)P.C_P = \left(\frac{\partial H}{\partial T}\right)_P = \left(\frac{\partial U}{\partial T}\right)_P + P\left(\frac{\partial V}{\partial T}\right)_P.
    • For an ideal gas: CP−CV=NkBC_P - C_V = Nk_{\mathrm{B}} (or nRnR per mole), so CP>CVC_P > C_V.

  3. When qP=ΔHq_P = \Delta H Fails

    • The relation holds only when PVPV work is the sole form of work. Non-PVPV work at constant pressure (e.g., electrical work in an electrochemical cell) breaks the equivalence.

  4. Standard States and Formation Enthalpies

    • Standard pressure: P∘=1 barP^\circ = 1\,\text{bar}; reference temperature typically 298.15 K.

    • Standard enthalpy of formation, ΔHf∘\Delta H_f^\circ: enthalpy change when 1 mol of compound is formed from elements in their standard states.

    • By convention, ΔHf∘=0\Delta H_f^\circ = 0 for elements in their standard states.

  5. Hess’s Law

    • Because HH is a state function, enthalpy changes are path-independent and additive:

    ΔHrxn∘=∑pνp ΔHf,p∘−∑rνr ΔHf,r∘.\Delta H_{\mathrm{rxn}}^\circ = \sum_{p} \nu_p \,\Delta H_{f,p}^\circ - \sum_{r} \nu_r \,\Delta H_{f,r}^\circ.
  6. First Law Toolkit Summary

    ConstraintRelevant state functionKey relation
    Constant VVUUqV=ΔUq_V = \Delta U
    Constant PPH=U+PVH = U + PVqP=ΔHq_P = \Delta H

2. Checklist of Most Important Equations

Below is a unified list of the major equations from Sections 3.1–3.3.

A. First Law of Thermodynamics

ΔU=q+w(finite),dU=δq+δw(differential).\Delta U = q + w \qquad\text{(finite)}, \qquad dU = \delta q + \delta w \qquad\text{(differential)}.

B. PVPV Work

δw=−Pext dV⟹w=−∫V1V2Pext dV.\delta w = -P_{\mathrm{ext}}\,dV \qquad\Longrightarrow\qquad w = -\int_{V_1}^{V_2} P_{\mathrm{ext}}\,dV.

C. First Law in (V,T)(V, T) Variables (for PVPV-only work)

δq=CV dT+[(∂U∂V)T+P]dV.\delta q = C_V\,dT + \left[\left(\frac{\partial U}{\partial V}\right)_T + P\right] dV.

D. Isothermal Reversible Work (ideal gas)

w=−nRTln⁡ ⁣(V2V1),q=−w=nRTln⁡ ⁣(V2V1).w = -nRT\ln\!\left(\frac{V_2}{V_1}\right), \qquad q = -w = nRT\ln\!\left(\frac{V_2}{V_1}\right).

E. Adiabatic Relations (ideal gas, reversible)

TVγ−1=const,PVγ=const,γ=CPCV.TV^{\gamma - 1} = \text{const}, \qquad PV^{\gamma} = \text{const}, \qquad \gamma = \frac{C_P}{C_V}.

F. Isochoric Process (dV=0dV = 0)

qV=ΔU=∫T1T2CV dT.q_V = \Delta U = \int_{T_1}^{T_2} C_V\,dT.

G. Enthalpy

H=U+PV.H = U + PV.

H. Heat Capacity at Constant Pressure

CP=(∂H∂T)P,ΔH=∫T1T2CP dT.C_P = \left(\frac{\partial H}{\partial T}\right)_P, \qquad \Delta H = \int_{T_1}^{T_2} C_P\,dT.

I. Hess’s Law

ΔHrxn∘=∑pνp ΔHf,p∘−∑rνr ΔHf,r∘.\Delta H_{\mathrm{rxn}}^\circ = \sum_{p} \nu_p\,\Delta H_{f,p}^\circ - \sum_{r} \nu_r\,\Delta H_{f,r}^\circ.

J. Microscopic First Law

dU=∑iEi dpi⏟δq  +  ∑ipi dEi⏟δw.dU = \underbrace{\sum_i E_i\, dp_i}_{\delta q} \;+\; \underbrace{\sum_i p_i\, dE_i}_{\delta w}.