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Summary of Thermodynamics and Thermochemistry

Jan 3, 2026

Overview

  • These notes are a collection of the basic principles of thermodynamics and thermochemistry.
  • Main topics: system-surroundings, properties, state and path functions, major thermodynamic processes, rules for work and heat, U/H/╬Ф, heat capacity, entropy, Gibbs energy and bomb calorimeter practice.
  • Goal: provide exam-level formulas, definitions and step-by-step solution methods.

System, Surroundings and Boundaries

  • System: the part of the universe we study (e.g., a cup of hot tea).
  • Surroundings: everything outside the system.
  • Boundary: the surface separating system and surroundings; can be real or imaginary.
  • Types of boundaries: adiabatic (no heat exchange), diathermic (heat exchange possible), rigid/non-rigid, permeable/impermeable.

System Types (open/closed/isolated)

  • Open system: mass and heat can change (╬Фm тЙа 0, q тЙа 0).
  • Closed system: mass does not change, heat can change (╬Фm = 0, q тЙа 0).
  • Isolated system: neither mass nor heat is exchanged (╬Фm = 0, q = 0).

Extensive and Intensive Properties

  • Extensive: depend on amount (mass, volume, U, H, S).
  • Intensive: do not depend on amount (T, p, mole fraction, pH).
  • Identification: if a property changes with scaling тЖТ extensive; per mole or specific тЖТ intensive; ratio of two extensive properties тЖТ intensive.

State Functions and Path Functions

  • State functions: P, V, T, U, H, S, G тАФ depend only on initial/final states; ╬ФU, ╬ФH etc.
  • Path functions: W, Q тАФ depend on the path; expressed with ╬┤Q, ╬┤W.
  • Infinitesimal changes: dU, dH (state); ╬┤Q, ╬┤W (path).

Thermodynamic Processes (definitions and formulas)

  • Isothermal (T constant): PV = constant; reversible W = - nRT ln(V2/V1); ╬ФU = 0 тЗТ Q = -W.
  • Isochoric / isovolumetric (V constant): ╬ФV = 0 тЗТ W = 0; Q = ╬ФU = n CV ╬ФT.
  • Isobaric (P constant): W = - P (V2 - V1); Q = ╬ФH = n CP ╬ФT.
  • Adiabatic (Q = 0): ╬ФU = W; reversible: PV^╬│ = constant, TV^(╬│-1) = constant; ╬│ = CP/CV, R = CP - CV; W = (P2V2 - P1V1)/(╬│ - 1) (with appropriate sign).
  • Cyclic process: start = end тЗТ all state function ╬Ф = 0 but Q_net and W_net are generally not 0.

Work (details, sign convention, formulas)

  • Infinitesimal work: ╬┤W = - P_ext dV (P_ext = external pressure).
  • Sign convention:
    • Q positive when the system absorbs heat; Q negative when it releases heat.
    • W negative when the system does work; W positive when work is done on the system.
  • Specifics:
    • Reversible isothermal: W = - nRT ln(V2/V1).
    • Irreversible (constant external P): W = - P_ext (V2 - V1).
    • On a PV graph W = area under the curve.
    • Free expansion (vacuum): P_ext = 0 тЗТ W = 0.

Internal Energy (U) and Enthalpy (H)

  • Internal energy U: the system's internal energy (translation, rotation, vibration, electronic). For an ideal gas U = function(T).
  • Enthalpy H = U + PV; both are state functions.
  • General relation: ╬ФH = ╬ФU + ╬Ф(PV); if P is constant then ╬ФH = ╬ФU + P ╬ФV.
  • For an ideal gas ╬Ф(PV) = nR ╬ФT тЗТ ╬ФH = ╬ФU + nR ╬ФT.
  • For changes in gaseous moles ╬ФH = ╬ФU + R T ╬Фn_gas (assuming constant T).

Heat Capacity

  • C = dq/dT; specific heat = per gram; molar heat capacity = per mole.
  • Constant-volume: ╬ФU = n CV ╬ФT.
  • Constant-pressure: ╬ФH = n CP ╬ФT.
  • Relation: CP - CV = R ; ╬│ = CP / CV.
  • Typical values:
    • Monoatomic: CV = 3/2 R, CP = 5/2 R, ╬│ = 5/3.
    • Diatomic: CV = 5/2 R, CP = 7/2 R, ╬│ = 7/5.
    • Polyatomic (approx): ╬│ тЙИ 4/3.

Mixtures (mixed heat capacity)

  • Molar average for mixtures:
    • CP_mix = (╬г ni CP,i) / (╬г ni) ; CV_mix = (╬г ni CV,i) / (╬г ni).
  • If ╬│_i are given: CV_i = R / (╬│_i - 1) then form the mixture; then ╬│_mix = CP_mix / CV_mix.

Thermochemistry тАФ Enthalpy and ways to get ╬ФH

  • ╬ФH_reaction = ╬г ╬ФHf(products) тИТ ╬г ╬ФHf(reactants).
  • Alternative: ╬ФH = Eact(fwd) тИТ Eact(bwd).
  • Combustion dataset: ╬ФH_reaction = ╬г(combustion of reactants) тИТ ╬г(combustion of products).
  • Bond energies: ╬ФH_reaction = ╬г(BDE broken) тИТ ╬г(BDE formed).
  • Conditions for heats of formation: 1 mol product, elements in most stable standard state, usually 298 K and 1 bar.

Entropy (╬ФS) тАФ properties and formulas

  • Qualitative: entropy = disorder; gas > liquid > solid.
  • Rules: increase in moles of gas тЖТ ╬ФS > 0; mixing increases ╬ФS; greater atomicity тЖТ larger S.
  • Spontaneity: ╬ФS_universe = ╬ФS_system + ╬ФS_surroundings; if >0 тЖТ spontaneous.
  • Mathematical:
    • dS = ╬┤Q_rev / T.
    • Ideal gas: ╬ФS = n Cv ln(T2/T1) + n R ln(V2/V1).
    • Special paths: isothermal: ╬ФS = n R ln(V2/V1); isochoric: ╬ФS = n Cv ln(T2/T1); isobaric: ╬ФS = n Cp ln(T2/T1).
    • Phase change: ╬ФS = ╬ФH_transition / T_transition.
    • Adiabatic reversible: ╬ФS = 0 (isentropic).

Gibbs Free Energy (╬ФG) and spontaneity

  • ╬ФG = ╬ФH тИТ T ╬ФS.
  • Rules: ╬ФG < 0 тЖТ spontaneous (at constant T,P); ╬ФG = 0 тЖТ equilibrium; ╬ФG > 0 тЖТ non-spontaneous.
  • Temperature dependence: if ╬ФH and ╬ФS have the same sign тЖТ spontaneity depends on T; cutoff T = ╬ФH/╬ФS.
  • Relation: ╬ФG┬░ = тИТ R T ln K.

Bomb Calorimeter тАФ principle and calculations (step-by-step)

  • Purpose: measure ╬ФE (internal energy change) from combustion/reaction at constant volume.
  • Basic steps:
    1. Calculate n from the given mass/moles.
    2. Total heat Q = C_total ├Ч ╬ФT (if C is given).
    3. If molar heat capacities are given use Q = ╬г (n_i ├Ч C_molar,i ├Ч ╬ФT).
    4. ╬ФU per mole = - Q / n_reactant (negative because the system released heat).
    5. If ╬ФH is needed and gaseous moles change then ╬ФH = ╬ФU + ╬Фn_gas ┬╖ R ┬╖ T (T in K).
  • In bomb calorimetry Q_released = C_cal ├Ч ╬ФT ; ╬ФE per mol тЙИ тИТ Q_released / n.
  • Use ╬Фn_gas and RT to adjust ╬ФU тЖТ ╬ФH.

Example: Benzoic acid bomb calorimeter (steps)

  • Given: benzoic acid 12.2 g (molar mass 122 g/mol тЖТ n = 0.100 mol тЙИ 1 mol if the problem states 1 mol).
  • C_total = 50 (units), ╬ФT = 77 тИТ 27 = 50┬░C.
  • Q = C ├Ч ╬ФT = 50 ├Ч 50 = 2500 (units); instructor example also showed 25000 J тАФ check units carefully.
  • ╬ФU per mol = - Q / n (negative sign).
  • Determine ╬Фn_gas (moles of gaseous products тИТ moles of gaseous reactants). Example had ╬Фn_gas = -1/2.
  • ╬ФH = ╬ФU + ╬Фn_gas ┬╖ R ┬╖ T (T = 300 K if 27┬░C).

Useful formulas (collected summary)

Quantity/resultSimple formula
Reversible isothermal workW = - n R T ln(V2/V1)
Irreversible constant P workW = - P_ext (V2 - V1)
Constant-volume heat╬ФU = n CV ╬ФT
Constant-pressure heat╬ФH = n CP ╬ФT
CP - CV relationCP - CV = R
Definition of ╬│╬│ = CP / CV
Relation ╬ФH and ╬ФU╬ФH = ╬ФU + ╬Фn_gas ┬╖ R ┬╖ T
Entropy change (ideal gas)╬ФS = n Cv ln(T2/T1) + n R ln(V2/V1)
Phase change entropy╬ФS = ╬ФH_transition / T_transition
Gibbs free energy╬ФG = ╬ФH тИТ T ╬ФS
Standard ╬ФG and K╬ФG┬░ = тИТ R T ln K
Bomb calorimetry heatQ = C_cal ├Ч ╬ФT ; ╬ФE тЙИ тИТ Q / n

Thermochemistry: Hess's Law, Bond Energies, Formation, Combustion

  • Hess's Law: the ╬ФH of a reaction is the sum of ╬ФH of the steps that lead to it.
  • Formation enthalpy rule: ╬ФH_reaction = ╬г ╬ФHf(products) тИТ ╬г ╬ФHf(reactants).
  • Combustion enthalpy: can use ╬ФH_reaction = ╬г (combustion reactants) тИТ ╬г (combustion products).
  • Bond method: broken bonds (positive) тИТ formed bonds (negative) = ╬ФH_reaction.

Action Items / Next Steps (practice suggestions)

  • Practice areas on PV graphs: areas and interconversion for isothermal, isobaric, isochoric, adiabatic curves.
  • Solve several numerical problems with reversible isothermal and irreversible constant-P work.
  • Memorize CP, CV, ╬│ values (mono-, di-, polyatomic) and use them in ╬ФU/╬ФH problems.
  • Thermochemistry: solve 3тАУ5 problems using ╬ФH formation/combustion and bond energy methods.
  • Bomb calorimeter problems: work through full steps C, ╬ФT тЖТ Q тЖТ ╬ФE per mol тЖТ ╬ФH adjustment.
  • Pay special attention to units (e.g., atm┬╖L тЖТ J; temperature in K when using R).