Thermodynamics
Chapter 12 | Class 11 Physics | CBSE 2025-26 Syllabus
Complete summary with laws of thermodynamics, heat engines, and thermodynamic processes
Essential concepts and memory tricks for mastering Thermodynamics
Zeroth Law of Thermodynamics and Thermal Equilibrium
If two systems are in thermal equilibrium with a third system, they are in thermal equilibrium with each other. This law defines temperature as a measurable quantity. Thermal equilibrium means no heat flow between systems despite being connected. Temperature is the property that determines thermal equilibrium - systems at same temperature are in thermal equilibrium.
First Law of Thermodynamics and Internal Energy
Energy cannot be created or destroyed, only transformed. ΔU = Q - W where ΔU is change in internal energy, Q is heat supplied to system, W is work done by system. Internal energy depends only on state, not path. Heat and work are path functions - they depend on how process occurs, not just initial and final states.
Thermodynamic Processes (Isothermal, Adiabatic, Isobaric, Isochoric)
Isothermal: constant temperature (ΔT = 0, ΔU = 0). Adiabatic: no heat exchange (Q = 0). Isobaric: constant pressure. Isochoric: constant volume (W = 0). Each process has specific P-V relationships and work formulas. Isothermal curve is less steep than adiabatic on P-V diagram because γ > 1.
Second Law of Thermodynamics and Entropy
Heat cannot spontaneously flow from cold to hot reservoir. No engine can convert 100% heat into work - some heat must be rejected. Entropy of isolated system always increases (ΔS ≥ 0). Reversible processes have ΔS = 0, irreversible have ΔS > 0. Entropy measures disorder in system.
Heat Engines and Refrigerators
Heat engine converts heat into work by operating between hot and cold reservoirs. Efficiency η = W/Q₁ = 1 - Q₂/Q₁ where Q₁ is heat input, Q₂ is heat rejected. Refrigerator moves heat from cold to hot reservoir using work. Coefficient of Performance (COP) = Q₂/W for refrigerator.
Carnot Engine and Carnot Cycle
Most efficient heat engine possible between two temperature reservoirs. Operates on reversible cycle with two isothermal and two adiabatic processes. Carnot efficiency η = 1 - T₂/T₁ depends only on reservoir temperatures. No real engine can exceed Carnot efficiency. Carnot refrigerator has maximum COP.
Thermodynamic State Variables and Equations
State variables (P, V, T, n) define system's thermodynamic state. Equation of state: PV = nRT for ideal gas. Extensive variables (V, n, U) depend on amount of substance. Intensive variables (P, T) are independent of amount. State functions depend only on current state, not history.
Real-World Applications and Examples
Car engines use Otto cycle (modified Carnot). Refrigerators and air conditioners are heat pumps. Steam engines and power plants convert heat to electricity. Biological processes follow thermodynamic laws. Weather systems driven by thermodynamic principles. Cooking processes involve heat transfer and thermodynamics.
All essential thermodynamics formulas with LaTeX equations and simple explanations
| Concept | Formula | Meaning in Simple Words | When to Use |
|---|---|---|---|
| First Law of Thermodynamics | \(\Delta U = Q - W\) | Change in internal energy equals heat added minus work done by system | For any thermodynamic process to relate heat, work, and internal energy |
| Alternative First Law Form | \(Q = \Delta U + W\) | Heat supplied equals change in internal energy plus work done by system | When calculating heat required for a process with known work and energy change |
| Work Done in General | \(W = \int P_{ext} dV\) | Work done by system equals integral of external pressure times volume change | For calculating work in any process where pressure varies with volume |
| Work Done in Isothermal Process | \(W = nRT \ln\left(\frac{V_2}{V_1}\right) = nRT \ln\left(\frac{P_1}{P_2}\right)\) | Work done in isothermal process depends logarithmically on volume or pressure ratio | For isothermal expansion or compression of ideal gas at constant temperature |
| Work Done in Adiabatic Process | \(W = \frac{nR(T_1 - T_2)}{\gamma - 1} = \frac{P_1V_1 - P_2V_2}{\gamma - 1}\) | Work done in adiabatic process relates to temperature difference and gamma | For adiabatic processes where no heat is exchanged with surroundings |
| Work Done in Isobaric Process | \(W = P(V_2 - V_1) = nR(T_2 - T_1)\) | Work done at constant pressure equals pressure times volume change | For processes occurring at constant pressure like atmospheric processes |
| Work Done in Isochoric Process | \(W = 0\) | No work done when volume remains constant | For constant volume processes like heating gas in rigid container |
| Adiabatic Process Relation | \(PV^\gamma = \text{constant} \text{ or } P_1V_1^\gamma = P_2V_2^\gamma\) | For adiabatic process, pressure times volume to power gamma remains constant | To relate pressure and volume in adiabatic processes |
| Adiabatic Temperature-Volume Relation | \(TV^{\gamma-1} = \text{constant} \text{ or } T_1V_1^{\gamma-1} = T_2V_2^{\gamma-1}\) | In adiabatic process, temperature times volume to power (gamma-1) is constant | To find temperature change in adiabatic expansion or compression |
| Mayer's Relation | \(C_P - C_V = R\) | Difference between molar heat capacities at constant pressure and volume equals gas constant | To relate heat capacities or calculate one when other is known |
| Heat Capacity Ratio | \(\gamma = \frac{C_P}{C_V}\) | Gamma is ratio of heat capacity at constant pressure to constant volume | For adiabatic process calculations and determining gas properties |
| Heat Engine Efficiency | \(\eta = \frac{W}{Q_1} = \frac{Q_1 - Q_2}{Q_1} = 1 - \frac{Q_2}{Q_1}\) | Efficiency equals work output divided by heat input, or fraction of heat converted to work | To calculate efficiency of any heat engine |
| Carnot Engine Efficiency | \(\eta_{Carnot} = 1 - \frac{T_2}{T_1}\) | Carnot efficiency depends only on absolute temperatures of hot and cold reservoirs | For maximum possible efficiency between two temperature reservoirs |
| Coefficient of Performance (Refrigerator) | \(COP_R = \frac{Q_2}{W} = \frac{Q_2}{Q_1 - Q_2}\) | COP is ratio of heat removed from cold reservoir to work input | To measure effectiveness of refrigerators and air conditioners |
| Carnot Refrigerator COP | \(COP_{Carnot} = \frac{T_2}{T_1 - T_2}\) | Maximum COP for refrigerator depends only on reservoir temperatures | For ideal refrigerator performance between two temperature reservoirs |
| Entropy Change | \(\Delta S = \frac{Q_{rev}}{T} \text{ for reversible process}\) | Entropy change equals heat exchanged reversibly divided by absolute temperature | To calculate entropy change in reversible thermodynamic processes |
Systematic approach to solve Thermodynamics problems efficiently
Identify the Thermodynamic Process Type
Determine if process is isothermal (T constant), adiabatic (Q = 0), isobaric (P constant), or isochoric (V constant). Look for keywords: 'insulated' suggests adiabatic, 'constant temperature' means isothermal, 'constant pressure' is isobaric, 'rigid container' implies isochoric.
Draw P-V Diagrams and State Diagrams
Sketch P-V diagram showing initial and final states. Mark the process path: isothermal (hyperbola), adiabatic (steeper curve), isobaric (horizontal line), isochoric (vertical line). This visual helps identify work done (area under curve) and process characteristics.
Apply First Law of Thermodynamics Correctly
Use ΔU = Q - W with proper sign conventions. Q > 0 when heat is added to system, W > 0 when system does work on surroundings. For isothermal process: ΔU = 0. For adiabatic: Q = 0. For isochoric: W = 0.
Calculate Work Done Using Appropriate Formulas
Choose correct work formula based on process type. Isothermal: W = nRT ln(V₂/V₁). Adiabatic: W = (P₁V₁ - P₂V₂)/(γ-1). Isobaric: W = P(V₂ - V₁). Isochoric: W = 0. Remember work is area under P-V curve.
Determine Heat Transfer and Internal Energy Changes
Calculate ΔU using ΔU = nCᵥΔT for ideal gas. For isothermal: ΔU = 0, so Q = W. For adiabatic: Q = 0, so ΔU = -W. For other processes, use first law: Q = ΔU + W. Always check energy conservation.
Apply Second Law for Heat Engines and Refrigerators
For heat engines: η = W/Q₁ = 1 - Q₂/Q₁, must be < ηCarnot = 1 - T₂/T₁. For refrigerators: COP = Q₂/W, must be < COPCarnot = T₂/(T₁-T₂). Check that entropy of universe increases (ΔS ≥ 0).
Check Conservation of Energy Throughout
Verify energy balance: Q₁ = W + Q₂ for heat engines. For cycles: ΔU = 0, so Qnet = Wnet. Check that total energy input equals total energy output. For refrigerators: W + Q₂ = Q₁.
Verify Results with Physical Reasoning
Check if results make physical sense: efficiency should be < 100%, temperatures in Kelvin should be positive, work done should match P-V diagram area, adiabatic curves steeper than isothermal. Compare with theoretical limits like Carnot efficiency.
Avoid these common errors to improve your exam performance
| Mistake | How to Avoid |
|---|---|
| Confusing sign conventions for work and heat | Remember: Q > 0 when heat flows TO system, W > 0 when system does work ON surroundings. Use ΔU = Q - W consistently. Heat added and work done by system are positive in this convention. |
| Wrong application of isothermal vs adiabatic formulas | Isothermal: T constant, use PV = constant, W = nRT ln(V₂/V₁). Adiabatic: Q = 0, use PVᵞ = constant, W = (P₁V₁-P₂V₂)/(γ-1). Don't mix up the equations or their conditions. |
| Mixing up efficiency and coefficient of performance | Efficiency η = W/Q₁ for heat engines (always < 1). COP = Q₂/W for refrigerators (can be > 1). Heat engines produce work, refrigerators consume work. Use correct formula for each device type. |
| Incorrect use of first law of thermodynamics | Always use ΔU = Q - W with proper signs. Don't confuse internal energy U with heat Q. Internal energy is state function, heat is path function. For complete cycles: ΔU = 0, so Q = W. |
| Forgetting to convert temperature to Kelvin | Always convert Celsius to Kelvin (K = °C + 273.15) before using in thermodynamic formulas. Carnot efficiency, gas laws, and entropy calculations require absolute temperature. Check units throughout calculation. |
| Misunderstanding P-V diagram slopes | Adiabatic curves are steeper than isothermal curves because γ > 1. Slope of isothermal: dP/dV = -P/V. Slope of adiabatic: dP/dV = -γP/V. Remember: steeper slope means adiabatic process. |
| Wrong calculation of work done in cyclic processes | Work done in complete cycle = area enclosed by P-V curve. For clockwise cycle: W > 0 (net work output). For counterclockwise: W < 0 (net work input). Don't just add work from individual processes. |
| Confusing internal energy with heat | Internal energy U is total energy of system (state function). Heat Q is energy transfer (path function). ΔU depends only on initial and final states, Q depends on process path. Don't use them interchangeably. |
| Incorrect application of Carnot engine formulas | Carnot efficiency η = 1 - T₂/T₁ uses absolute temperatures in Kelvin. This is maximum possible efficiency between reservoirs. Real engines have lower efficiency due to irreversibilities. Apply only to ideal reversible engines. |
| Missing the relationship between Cp and Cv | Mayer's relation: Cₚ - Cᵥ = R for ideal gas. γ = Cₚ/Cᵥ where γ > 1 always. For monatomic gas: Cᵥ = (3/2)R, Cₚ = (5/2)R, γ = 5/3. Use correct values for different gas types. |
Quick memory aids and essential information for last-minute revision
First & Second Law Quick Formulas
- First Law: ΔU = Q - W
- Second Law: Heat flows hot → cold spontaneously
- Carnot efficiency: η = 1 - T₂/T₁
- No engine can be 100% efficient
Work Done in Four Processes
- Isothermal: W = nRT ln(V₂/V₁)
- Adiabatic: W = (P₁V₁ - P₂V₂)/(γ-1)
- Isobaric: W = P(V₂ - V₁) = nR(T₂ - T₁)
- Isochoric: W = 0 (no volume change)
Heat Engine & Refrigerator Formulas
- Engine efficiency: η = W/Q₁ = 1 - Q₂/Q₁
- Refrigerator COP: COP = Q₂/W
- Energy conservation: Q₁ = W + Q₂
- Max efficiency = Carnot efficiency
Carnot Cycle Key Relationships
- Carnot efficiency: η = 1 - T₂/T₁
- Carnot COP: COP = T₂/(T₁ - T₂)
- Four processes: 2 isothermal + 2 adiabatic
- Reversible cycle with maximum efficiency
Important Constants & Relations
- Mayer's relation: Cₚ - Cᵥ = R
- γ = Cₚ/Cᵥ (always > 1)
- Monatomic: γ = 5/3, Diatomic: γ = 7/5
- R = 8.314 J/(mol·K)
P-V Diagram Identification
- Isothermal: Hyperbola (PV = constant)
- Adiabatic: Steeper curve (PVᵞ = constant)
- Isobaric: Horizontal line (P = constant)
- Isochoric: Vertical line (V = constant)
Problem Type Recognition
- 'Insulated' or 'rapid' → Adiabatic (Q = 0)
- 'Constant temperature' → Isothermal (ΔU = 0)
- 'Rigid container' → Isochoric (W = 0)
- 'Open to atmosphere' → Isobaric
Exam Strategy Tips
- Always convert temperatures to Kelvin
- Draw P-V diagrams for visualization
- Check energy conservation in cycles
- Verify efficiency < Carnot limit
