This comprehensive guide is designed to equip JEE Main aspirants with an exhaustive formula sheet and conceptual understanding of Thermodynamics and Heat Transfer. Mastering this chapter is crucial for securing good ranks, as it frequently features high-scoring questions.
JEE Main Physics: Thermodynamics & Heat Transfer Formula Sheet
Thermodynamics is a fundamental branch of physics that deals with heat and its relation to other forms of energy and work. Heat Transfer, a closely related field, focuses on the mechanisms by which thermal energy moves from one place to another. Together, these topics form a significant portion of the JEE Main Physics syllabus, testing concepts from basic gas laws to complex thermodynamic processes and heat transfer modes.
Exam Weightage Analysis
Historically, Thermodynamics and Heat Transfer contribute a substantial number of questions to the JEE Main Physics section. Typically, 2-3 questions, sometimes even 4, can be expected from this unit, making it one of the most high-scoring and important chapters. These questions often involve applying specific formulas, understanding conceptual relationships between thermodynamic variables, and analyzing heat transfer scenarios. Mastering this chapter can secure 8-16 marks, a crucial factor in competitive exams.
Key Concepts and Definitions
Before diving into formulas, let's solidify the fundamental definitions and concepts.
- System: A region of the universe chosen for study.
- Open System: Exchanges both energy and matter with its surroundings. (e.g., boiling water in an open pot)
- Closed System: Exchanges energy but not matter with its surroundings. (e.g., gas in a sealed cylinder with a piston)
- Isolated System: Exchanges neither energy nor matter with its surroundings. (e.g., an ideal thermoflask)
- Surroundings: Everything outside the system that can interact with it.
- Boundary: The real or imaginary surface separating the system from its surroundings.
- Thermodynamic State: Defined by a set of measurable properties like pressure (P), volume (V), temperature (T), and number of moles (n).
- State Variables (or Point Functions): Properties that depend only on the initial and final states of the system, not on the path taken. Examples: P, V, T, U (internal energy), S (entropy).
- Path Variables (or Path Functions): Properties that depend on the path taken between the initial and final states. Examples: Q (heat), W (work).
- Extensive Properties: Depend on the amount of matter in the system. Examples: Mass, Volume, Internal Energy.
- Intensive Properties: Independent of the amount of matter. Examples: Pressure, Temperature, Density.
- Thermodynamic Process: A change in the state of a system.
- Isothermal Process: Temperature remains constant ($dT=0$, $T=$ constant).
- Isobaric Process: Pressure remains constant ($dP=0$, $P=$ constant).
- Isochoric Process (Isovolumetric): Volume remains constant ($dV=0$, $V=$ constant).
- Adiabatic Process: No heat exchange ($dQ=0$, Q = constant).
- Cyclic Process: The system returns to its initial state.
- Quasi-static Process: A process that proceeds infinitely slowly through a series of equilibrium states.
- Equilibrium: A state where no macroscopic changes are observed in the system and no net flows of matter or energy occur.
- Thermal Equilibrium: Uniform temperature throughout.
- Mechanical Equilibrium: Uniform pressure throughout (no unbalanced forces).
- Chemical Equilibrium: No net change in chemical composition.
- Internal Energy (U): The total energy contained within a thermodynamic system, excluding the kinetic and potential energy of the system as a whole. For an ideal gas, it depends only on temperature.
Thermodynamics Formulas
1. Zeroth Law of Thermodynamics
States that if two systems are each in thermal equilibrium with a third system, then they are in thermal equilibrium with each other. This law forms the basis of temperature measurement.
2. First Law of Thermodynamics (Conservation of Energy)
The change in internal energy ($\Delta U$) of a system is equal to the heat ($Q$) added to the system minus the work ($W$) done by the system.
$$ \Delta U = Q - W $$
Sign Conventions:
- $Q > 0$: Heat added to the system.
- $Q < 0$: Heat removed from the system.
- $W > 0$: Work done by the system (expansion).
- $W < 0$: Work done on the system (compression).
Infinitesimal Change: $$ dU = dQ - dW $$ where $dW = P dV$ for quasi-static processes. $$ dU = dQ - P dV $$
3. Work Done by a Gas
Work done by a gas during a volume change from $V_i$ to $V_f$ at pressure $P$:
$$ W = \int_{V_i}^{V_f} P dV $$
For specific processes, this integral simplifies:
Isobaric Process ($P = \text{constant}$): $$ W = P \int_{V_i}^{V_f} dV = P(V_f - V_i) $$ If $V_f > V_i$, $W > 0$ (work done by the system). If $V_f < V_i$, $W < 0$ (work done on the system).
Isochoric Process ($V = \text{constant}$, $dV = 0$): $$ W = 0 $$
4. Internal Energy of an Ideal Gas
For an ideal gas, internal energy ($U$) depends only on temperature ($T$).
$$ U = n C_v T $$ $$ \Delta U = n C_v \Delta T $$
where $n$ is the number of moles and $C_v$ is the molar specific heat at constant volume.
Degrees of Freedom ($f$): The number of independent ways in which a molecule can absorb energy.
| Gas Type | Degrees of Freedom ($f$) | $C_v = \frac{f}{2}R$ | $C_p = (\frac{f}{2}+1)R$ | $\gamma = \frac{C_p}{C_v} = 1 + \frac{2}{f}$ |
|---|---|---|---|---|
| Monoatomic | 3 (translational) | $\frac{3}{2}R$ | $\frac{5}{2}R$ | $\frac{5}{3} \approx 1.67$ |
| Diatomic | 5 (3 trans, 2 rot) | $\frac{5}{2}R$ | $\frac{7}{2}R$ | $\frac{7}{5} = 1.4$ |
| Polyatomic | 6 (3 trans, 3 rot) | $3R$ | $4R$ | $\frac{4}{3} \approx 1.33$ |
| (non-linear) |
- Universal Gas Constant (R): $R = 8.314 \text{ J mol}^{-1} \text{ K}^{-1}$
5. Molar Specific Heats ($C_p$ and $C_v$)
- Specific Heat at Constant Volume ($C_v$): $$ C_v = \frac{1}{n} \left(\frac{dQ}{dT}\right)_V $$
- Specific Heat at Constant Pressure ($C_p$): $$ C_p = \frac{1}{n} \left(\frac{dQ}{dT}\right)_P $$
- Relation between $C_p$ and $C_v$ (Mayer's Formula): $$ C_p - C_v = R $$
- Adiabatic Index ($\gamma$): $$ \gamma = \frac{C_p}{C_v} $$
6. Thermodynamic Processes Summarized
Let's consolidate the key formulas for different processes:
| Process | Condition | First Law ($Q - W = \Delta U$) | Work Done ($W$) | Change in Internal Energy ($\Delta U$) | Heat Supplied ($Q$) | P-V Relation | T-V Relation | P-T Relation |
|---|---|---|---|---|---|---|---|---|
| Isothermal | $T = \text{const}$ | $Q = W$ | $nRT \ln\left(\frac{V_f}{V_i}\right)$ or $P_iV_i \ln\left(\frac{V_i}{V_f}\right)$ | $0$ | $nRT \ln\left(\frac{V_f}{V_i}\right)$ or $P_iV_i \ln\left(\frac{P_i}{P_f}\right)$ | $PV = \text{const}$ ($P_iV_i=P_fV_f$) | $TV^{0} = \text{const}$ | $P/T = \text{const}$ |
| Isobaric | $P = \text{const}$ | $Q = W + \Delta U$ | $P(V_f - V_i) = nR\Delta T$ | $nC_v\Delta T$ | $nC_p\Delta T$ | $V/T = \text{const}$ ($V_i/T_i=V_f/T_f$) | $T/V = \text{const}$ | $P^{0}T = \text{const}$ |
| Isochoric | $V = \text{const}$ | $Q = \Delta U$ | $0$ | $nC_v\Delta T$ | $nC_v\Delta T$ | $P/T = \text{const}$ ($P_i/T_i=P_f/T_f$) | $T/P = \text{const}$ | $P/T = \text{const}$ |
| Adiabatic | $Q = 0$ | $-W = \Delta U$ | $-\Delta U = -nC_v\Delta T = \frac{P_fV_f-P_iV_i}{1-\gamma}$ | $nC_v\Delta T = \frac{P_iV_i-P_fV_f}{\gamma-1}$ | $0$ | $PV^{\gamma} = \text{const}$ | $TV^{\gamma-1} = \text{const}$ | $P^{1-\gamma}T^{\gamma} = \text{const}$ or $T P^{(1-\gamma)/\gamma} = \text{const}$ |
Note on Work Done for Adiabatic Process: The work done can also be expressed as $W = \frac{P_iV_i - P_fV_f}{\gamma - 1}$.
7. Cyclic Process
For a cyclic process, the system returns to its initial state.
- $\Delta U = 0$
- $Q_{net} = W_{net}$ (net heat supplied equals net work done)
- Work done is the area enclosed by the cycle on a P-V diagram. Clockwise cycle implies $W_{net} > 0$, counter-clockwise implies $W_{net} < 0$.
8. Second Law of Thermodynamics
States that the entropy of an isolated system never decreases. It always increases or remains constant in spontaneous processes. It also defines the direction of heat flow.
- Kelvin-Planck Statement: It is impossible to construct a device which operates in a cycle and produces no other effect than the extraction of heat from a single reservoir and the performance of an equivalent amount of work.
- Clausius Statement: It is impossible to construct a device which operates in a cycle and produces no other effect than the transfer of heat from a colder body to a hotter body.
9. Heat Engines, Refrigerators, and Heat Pumps
These devices operate on thermodynamic cycles.
- Heat Engine: Converts heat energy into mechanical work.
- Efficiency ($\eta$): $$ \eta = \frac{W}{Q_H} = 1 - \frac{Q_L}{Q_H} $$ where $Q_H$ is heat absorbed from hot reservoir, $Q_L$ is heat rejected to cold reservoir, $W$ is work done.
- Carnot Engine (Ideal Heat Engine): Operates between two temperatures $T_H$ (hot) and $T_L$ (cold).
- Maximum theoretical efficiency: $$ \eta_C = 1 - \frac{T_L}{T_H} $$
- For Carnot cycle, $\frac{Q_L}{Q_H} = \frac{T_L}{T_H}$
- Refrigerator/Heat Pump: Transfers heat from a colder body to a hotter body with work input.
- Coefficient of Performance (COP) for Refrigerator ($\beta$): $$ \beta_{ref} = \frac{\text{Heat extracted from cold reservoir}}{\text{Work input}} = \frac{Q_L}{W} = \frac{Q_L}{Q_H - Q_L} $$
- Coefficient of Performance (COP) for Heat Pump ($\beta'$): $$ \beta'_{HP} = \frac{\text{Heat delivered to hot reservoir}}{\text{Work input}} = \frac{Q_H}{W} = \frac{Q_H}{Q_H - Q_L} $$
- Relation: $\beta'{HP} = 1 + \beta{ref}$
- Carnot Refrigerator/Heat Pump: $$ \beta_{ref, C} = \frac{T_L}{T_H - T_L} $$ $$ \beta'_{HP, C} = \frac{T_H}{T_H - T_L} $$
Heat Transfer Formulas
Heat transfer is the exchange of thermal energy between physical systems. There are three primary modes: Conduction, Convection, and Radiation.
1. Conduction
Transfer of heat through direct contact of particles, without macroscopic movement of matter.
Fourier's Law of Heat Conduction: $$ \frac{dQ}{dt} = -kA \frac{dT}{dx} $$ where $\frac{dQ}{dt}$ is the rate of heat flow (thermal current), $k$ is the thermal conductivity of the material, $A$ is the cross-sectional area, and $\frac{dT}{dx}$ is the temperature gradient. The negative sign indicates heat flows in the direction of decreasing temperature.
For a rod of length $L$ and uniform cross-section $A$, with temperatures $T_1$ and $T_2$ at ends ($T_1 > T_2$): $$ H = \frac{dQ}{dt} = \frac{kA(T_1 - T_2)}{L} $$ Here, thermal resistance $R_{th} = \frac{L}{kA}$. $$ H = \frac{T_1 - T_2}{R_{th}} $$
Thermal Resistances in Series: For layers stacked side-by-side. $$ R_{th,eq} = R_{th,1} + R_{th,2} + \dots = \frac{L_1}{k_1A} + \frac{L_2}{k_2A} + \dots $$ $$ H = \frac{T_1 - T_n}{R_{th,eq}} $$
Thermal Resistances in Parallel: For layers arranged parallel such that heat flows through them simultaneously. $$ \frac{1}{R_{th,eq}} = \frac{1}{R_{th,1}} + \frac{1}{R_{th,2}} + \dots $$ $$ H = (T_1 - T_2) \left( \frac{kA_1}{L} + \frac{kA_2}{L} + \dots \right) $$
2. Convection
Transfer of heat by the movement of fluids (liquids or gases).
- Newton's Law of Cooling (for forced convection): $$ \frac{dQ}{dt} = hA(T_s - T_f) $$ where $h$ is the convective heat transfer coefficient, $A$ is the surface area, $T_s$ is the surface temperature, and $T_f$ is the fluid temperature.
- Natural Convection: Occurs due to density differences caused by temperature variations.
- Forced Convection: Occurs due to external means like a fan or pump.
3. Radiation
Transfer of heat through electromagnetic waves, requiring no medium.
Stefan-Boltzmann Law: The total energy radiated per unit surface area of a black body across all wavelengths per unit time is directly proportional to the fourth power of the black body's absolute temperature ($T$). $$ P = \frac{dQ}{dt} = \sigma A T^4 $$ where $P$ is the radiated power, $\sigma$ is the Stefan-Boltzmann constant ($\sigma = 5.67 \times 10^{-8} \text{ W m}^{-2} \text{ K}^{-4}$), $A$ is the surface area, and $T$ is the absolute temperature in Kelvin.
For a non-black body (emissivity $e$): $$ P_{non-black} = e \sigma A T^4 $$ where $e$ is the emissivity ($0 < e \le 1$). For a perfect black body, $e=1$.
Net heat radiated from a body at temperature $T$ in surroundings at $T_0$: $$ P_{net} = e \sigma A (T^4 - T_0^4) $$
Kirchhoff's Law of Radiation: For a given temperature and wavelength, the emissivity ($e$) of a body is equal to its absorptivity ($a$). Good emitters are good absorbers. $$ e(\lambda, T) = a(\lambda, T) $$
Wien's Displacement Law: The wavelength ($\lambda_m$) at which a black body radiates maximum energy is inversely proportional to its absolute temperature ($T$). $$ \lambda_m T = b $$ where $b$ is Wien's constant ($b = 2.898 \times 10^{-3} \text{ m K}$).
4. Newton's Law of Cooling (Approximate for radiation)
When the temperature difference between the body and surroundings is small ($T - T_0 = \Delta T \ll T_0$): $$ \frac{dQ}{dt} = -k'(T - T_0) $$ where $k'$ is a constant related to $e, A, \sigma, T_0$. This means the rate of cooling is proportional to the temperature difference.
Calorimetry and Phase Changes
- Heat required to change temperature of a substance: $$ Q = mc\Delta T $$ where $m$ is mass, $c$ is specific heat capacity, $\Delta T$ is change in temperature.
- Heat required for phase change (latent heat):
$$ Q = mL $$
where $L$ is latent heat (e.g., $L_f$ for fusion, $L_v$ for vaporization).
- Specific heat capacity of water: $c_w = 4200 \text{ J kg}^{-1} \text{ K}^{-1} = 1 \text{ cal g}^{-1} \text{ }^\circ\text{C}^{-1}$
- Latent heat of fusion of ice: $L_f = 3.34 \times 10^5 \text{ J kg}^{-1}$
- Latent heat of vaporization of water: $L_v = 2.26 \times 10^6 \text{ J kg}^{-1}$
Solved Examples
Let's work through some examples to illustrate the application of these formulas.
Example 1: Work Done in an Isothermal Expansion
A sample of 2 moles of an ideal gas at $27^\circ \text{C}$ expands isothermally and reversibly from a volume of $10 \text{ dm}^3$ to $20 \text{ dm}^3$. Calculate the work done by the gas. ($R = 8.314 \text{ J mol}^{-1} \text{ K}^{-1}$. $1 \text{ dm}^3 = 1 \text{ L}$).
Solution:
Identify the given values:
- Number of moles, $n = 2 \text{ mol}$
- Initial temperature, $T = 27^\circ \text{C} = 27 + 273 = 300 \text{ K}$ (isothermal process, so T is constant)
- Initial volume, $V_i = 10 \text{ dm}^3 = 10 \text{ L}$
- Final volume, $V_f = 20 \text{ dm}^3 = 20 \text{ L}$
- Gas constant, $R = 8.314 \text{ J mol}^{-1} \text{ K}^{-1}$
Recall the formula for work done in an isothermal reversible expansion: $$ W = nRT \ln\left(\frac{V_f}{V_i}\right) $$
Substitute the values into the formula: $$ W = (2 \text{ mol}) \times (8.314 \text{ J mol}^{-1} \text{ K}^{-1}) \times (300 \text{ K}) \times \ln\left(\frac{20 \text{ L}}{10 \text{ L}}\right) $$ $$ W = 2 \times 8.314 \times 300 \times \ln(2) $$
Calculate the natural logarithm of 2: $\ln(2) \approx 0.693$
Perform the multiplication: $$ W = 2 \times 8.314 \times 300 \times 0.693 $$ $$ W = 16.628 \times 207.9 $$ $$ W \approx 3457.7 \text{ J} $$
Answer: The work done by the gas is approximately $3457.7 \text{ J}$. Since $W > 0$, work is done by the system.
Example 2: Efficiency of a Heat Engine
A Carnot engine operates between $600 \text{ K}$ and $300 \text{ K}$. If it absorbs $1000 \text{ J}$ of heat from the source in each cycle, calculate the work done per cycle and the heat rejected to the sink.
Solution:
Identify the given values:
- Hot reservoir temperature, $T_H = 600 \text{ K}$
- Cold reservoir temperature, $T_L = 300 \text{ K}$
- Heat absorbed from source, $Q_H = 1000 \text{ J}$
Calculate the efficiency of the Carnot engine: $$ \eta_C = 1 - \frac{T_L}{T_H} $$ $$ \eta_C = 1 - \frac{300 \text{ K}}{600 \text{ K}} = 1 - 0.5 = 0.5 $$ The efficiency is 0.5 or 50%.
Calculate the work done per cycle using the efficiency formula: $$ \eta = \frac{W}{Q_H} $$ $$ W = \eta \times Q_H = 0.5 \times 1000 \text{ J} = 500 \text{ J} $$
Calculate the heat rejected to the sink ($Q_L$) using the first law of thermodynamics for a cyclic process ($W = Q_H - Q_L$): $$ Q_L = Q_H - W $$ $$ Q_L = 1000 \text{ J} - 500 \text{ J} = 500 \text{ J} $$
Answer: The work done per cycle is $500 \text{ J}$, and the heat rejected to the sink is $500 \text{ J}$.
Example 3: Thermal Conduction through a Compound Wall
An iron rod and a copper rod are joined end-to-end. Both have the same cross-sectional area and length. The free end of the iron rod is maintained at $T_1 = 100^\circ \text{C}$ and the free end of the copper rod is maintained at $T_2 = 0^\circ \text{C}$. Find the temperature of the junction. Given: thermal conductivity of iron ($k_{Fe}$) = $79 \text{ W m}^{-1} \text{ K}^{-1}$, thermal conductivity of copper ($k_{Cu}$) = $398 \text{ W m}^{-1} \text{ K}^{-1}$.
Solution:
Identify the setup: Two rods in series, same length ($L$), same cross-sectional area ($A$).
Principle: In steady state, the rate of heat flow through each rod is the same. Let $T_j$ be the temperature of the junction. Rate of heat flow through iron rod ($H_{Fe}$) = Rate of heat flow through copper rod ($H_{Cu}$). $$ H_{Fe} = \frac{k_{Fe} A (T_1 - T_j)}{L} $$ $$ H_{Cu} = \frac{k_{Cu} A (T_j - T_2)}{L} $$
Equate the heat flow rates: $$ \frac{k_{Fe} A (T_1 - T_j)}{L} = \frac{k_{Cu} A (T_j - T_2)}{L} $$ Since $A$ and $L$ are the same, they cancel out: $$ k_{Fe} (T_1 - T_j) = k_{Cu} (T_j - T_2) $$
Substitute the given values:
- $k_{Fe} = 79 \text{ W m}^{-1} \text{ K}^{-1}$
- $k_{Cu} = 398 \text{ W m}^{-1} \text{ K}^{-1}$
- $T_1 = 100^\circ \text{C}$
- $T_2 = 0^\circ \text{C}$
$$ 79 (100 - T_j) = 398 (T_j - 0) $$ $$ 7900 - 79 T_j = 398 T_j $$ $$ 7900 = 398 T_j + 79 T_j $$ $$ 7900 = 477 T_j $$
Solve for $T_j$: $$ T_j = \frac{7900}{477} \approx 16.56^\circ \text{C} $$
Answer: The temperature of the junction is approximately $16.56^\circ \text{C}$.
Example 4: Adiabatic Process
One mole of an ideal monoatomic gas at an initial temperature of $300 \text{ K}$ expands adiabatically from $V$ to $2V$. Calculate the final temperature of the gas. ($R = 8.314 \text{ J mol}^{-1} \text{ K}^{-1}$).
Solution:
Identify the given values:
- Number of moles, $n = 1 \text{ mol}$
- Initial temperature, $T_1 = 300 \text{ K}$
- Initial volume, $V_1 = V$
- Final volume, $V_2 = 2V$
- Process: Adiabatic
- Gas type: Monoatomic ideal gas
Determine $\gamma$ for a monoatomic gas: For a monoatomic gas, $f=3$. $$ \gamma = 1 + \frac{2}{f} = 1 + \frac{2}{3} = \frac{5}{3} $$
Recall the formula for an adiabatic process relating T and V: $$ T_1 V_1^{\gamma-1} = T_2 V_2^{\gamma-1} $$
Rearrange to solve for $T_2$: $$ T_2 = T_1 \left(\frac{V_1}{V_2}\right)^{\gamma-1} $$
Substitute the values: $$ T_2 = 300 \text{ K} \left(\frac{V}{2V}\right)^{\frac{5}{3}-1} $$ $$ T_2 = 300 \text{ K} \left(\frac{1}{2}\right)^{\frac{2}{3}} $$ $$ T_2 = 300 \text{ K} \times \frac{1}{(2^{1/3})^2} = 300 \text{ K} \times \frac{1}{(\sqrt[3]{2})^2} $$ Since $2^{1/3} \approx 1.2599$, $2^{2/3} \approx (1.2599)^2 \approx 1.587$: $$ T_2 = 300 \text{ K} \times \frac{1}{1.587} $$ $$ T_2 \approx 300 \text{ K} \times 0.6301 \approx 189.03 \text{ K} $$
Answer: The final temperature of the gas is approximately $189.03 \text{ K}$.
Example 5: Radiation and Net Heat Loss
A metallic sphere of radius $R$ is heated to a temperature $T$ and placed in a black enclosure at temperature $T_0$. If the emissivity of the sphere is $e$, calculate the net rate of heat loss from the sphere.
Solution:
Identify the given information:
- Radius of sphere = $R$
- Surface area of sphere, $A = 4\pi R^2$
- Temperature of sphere = $T$ (absolute temperature)
- Temperature of enclosure = $T_0$ (absolute temperature)
- Emissivity of sphere = $e$
- Stefan-Boltzmann constant = $\sigma$
Recall the formula for net heat radiated: The net rate of heat loss (power radiated) from a body at temperature $T$ in surroundings at $T_0$ is given by: $$ P_{net} = e \sigma A (T^4 - T_0^4) $$
Substitute the surface area of the sphere: $$ P_{net} = e \sigma (4\pi R^2) (T^4 - T_0^4) $$
Answer: The net rate of heat loss from the sphere is $4 \pi R^2 e \sigma (T^4 - T_0^4)$.
Example 6: Calorimetry - Mixing Ice and Water
$20 \text{ g}$ of ice at $0^\circ \text{C}$ is mixed with $50 \text{ g}$ of water at $40^\circ \text{C}$ in an insulated container. Calculate the final temperature of the mixture. Given: Specific heat of water ($c_w$) = $4.2 \text{ J g}^{-1} \text{ }^\circ\text{C}^{-1}$, Latent heat of fusion of ice ($L_f$) = $336 \text{ J g}^{-1}$.
Solution:
Identify the given values:
- Mass of ice, $m_{ice} = 20 \text{ g}$
- Initial temperature of ice, $T_{ice} = 0^\circ \text{C}$
- Mass of water, $m_{water} = 50 \text{ g}$
- Initial temperature of water, $T_{water} = 40^\circ \text{C}$
- $c_w = 4.2 \text{ J g}^{-1} \text{ }^\circ\text{C}^{-1}$
- $L_f = 336 \text{ J g}^{-1}$
Assume the final temperature is above $0^\circ \text{C}$ and calculate heat required (for ice) and heat released (by water).
Heat required by ice to melt at $0^\circ \text{C}$: $$ Q_1 = m_{ice} L_f = 20 \text{ g} \times 336 \text{ J g}^{-1} = 6720 \text{ J} $$
Maximum heat released by water to cool down to $0^\circ \text{C}$: $$ Q_2 = m_{water} c_w (T_{water} - 0^\circ \text{C}) = 50 \text{ g} \times 4.2 \text{ J g}^{-1} \text{ }^\circ\text{C}^{-1} \times (40 - 0)^\circ \text{C} $$ $$ Q_2 = 50 \times 4.2 \times 40 = 8400 \text{ J} $$
Compare $Q_1$ and $Q_2$: Since $Q_2 (8400 \text{ J})$ is greater than $Q_1 (6720 \text{ J})$, all ice will melt, and the final temperature will be greater than $0^\circ \text{C}$.
Calculate the remaining heat available after ice melts: $$ Q_{remaining} = Q_2 - Q_1 = 8400 \text{ J} - 6720 \text{ J} = 1680 \text{ J} $$ This remaining heat will raise the temperature of the total mass of water.
Calculate the final mass of water: $$ m_{total_water} = m_{ice} + m_{water} = 20 \text{ g} + 50 \text{ g} = 70 \text{ g} $$
Calculate the final temperature ($T_f$): The $1680 \text{ J}$ of heat will raise the temperature of $70 \text{ g}$ of water from $0^\circ \text{C}$ to $T_f$. $$ Q_{remaining} = m_{total_water} c_w (T_f - 0^\circ \text{C}) $$ $$ 1680 \text{ J} = 70 \text{ g} \times 4.2 \text{ J g}^{-1} \text{ }^\circ\text{C}^{-1} \times T_f $$ $$ 1680 = 294 T_f $$ $$ T_f = \frac{1680}{294} \approx 5.71^\circ \text{C} $$
Answer: The final temperature of the mixture is approximately $5.71^\circ \text{C}$.
Common Mistakes to Avoid
- Sign Conventions: The most frequent error in thermodynamics is incorrect sign usage for $Q$ and $W$.
- $Q$ (heat): Positive when entering the system, negative when leaving.
- $W$ (work): Positive when done by the system (expansion), negative when done on the system (compression). The JEE Main typically follows this convention. Always double-check problem statements for any specific convention.
- Units: Ensure consistency in units. Convert temperatures to Kelvin for thermodynamics formulas (especially Carnot efficiency, ideal gas law, and radiation formulas) and work/heat units to Joules.
- Ideal Gas Assumptions: Remember that $U$ depends only on $T$ for ideal gases. $\Delta U = n C_v \Delta T$ is always true for ideal gases, regardless of the process.
- $\gamma$ values: Memorize $\gamma$ values for monoatomic, diatomic, and polyatomic gases. Be aware that for diatomic gases, at very high temperatures, vibrational degrees of freedom can be excited, changing $\gamma$. However, for JEE Main, generally only translational and rotational degrees of freedom are considered unless specified.
- Isothermal vs. Adiabatic: Don't confuse the work done and P-V-T relations for these two processes. An adiabatic process has no heat exchange, while an isothermal process has constant temperature.
- Thermal vs. Electrical Analogy: While thermal resistance is analogous to electrical resistance, carefully apply formulas to series and parallel combinations.
- Blackbody vs. Greybody: Remember to include emissivity ($e$) for non-black bodies in radiation calculations.
- Newton's Law of Cooling Approximation: Use this law only for small temperature differences. For large differences, employ the Stefan-Boltzmann law.
- Heat Capacity vs. Specific Heat vs. Molar Heat Capacity: Understand the distinction between $C$ (heat capacity), $c$ (specific heat capacity), and $C_p, C_v$ (molar specific heat capacities), and use the correct one as per the problem.
Memory Tricks / Mnemonics
- Work Done mnemonic (P-V graph): "Area Under the Curve, Work, Work, Work!" (The area under the P-V curve represents work done).
- Adiabatic Relations "TV, PV, PT":
- $T V^{\gamma-1} = \text{const}$ (TV)
- $P V^{\gamma} = \text{const}$ (PV)
- $P^{1-\gamma} T^{\gamma} = \text{const}$ (PT, or $T P^{(1-\gamma)/\gamma} = \text{const}$)
- Mayer's Formula: "Cp is greater than Cv by R" ($C_p - C_v = R$). The pressure system needs more heat to raise temperature because it also does external work.
- Carnot Engine Efficiency: "Cold over Hot, and one minus that!" ($\eta_C = 1 - T_{cold}/T_{hot}$). The ideal efficiency always depends on temperature ratios.
- First Law Sign Convention: Think of your bank account.
- Deposits (heat ADDED to system, $Q_{in}$): +Q
- Withdrawals (heat REMOVED from system, $Q_{out}$): -Q
- Income (work DONE BY system, $W_{by}$): +W
- Expenses (work DONE ON system, $W_{on}$): -W
- $\Delta U = Q - W$ (as per JEE Convention, $W$ = work done BY the system)
- If you use $\Delta U = Q + W$, then $W$ must be work done ON the system. Be consistent!
Previous Year Question (PYQ) Patterns
JEE Main questions from Thermodynamics often involve:
- Calculations of Work, Heat, and Internal Energy Change: For various processes (isothermal, isobaric, isochoric, adiabatic), students are asked to calculate $Q$, $W$, or $\Delta U$. These are direct formula applications.
- P-V Diagrams: Interpretation of P-V diagrams to find work done (area under curve), identify processes, and analyze cyclic processes. Often combined with the First Law.
- Carnot Engine and Refrigerator: Questions on efficiency/COP, heat absorbed/rejected, and work done based on reservoir temperatures.
- Heat Transfer:
- Conduction: Calculation of thermal resistance, junction temperature in series/parallel combinations of rods.
- Radiation: Application of Stefan-Boltzmann law for net heat loss/gain, or Wien's displacement law relating peak wavelength and temperature.
- Calorimetry: Problems involving phase changes, specific heat capacities, and determination of final mixture temperature.
- Degrees of Freedom and Specific Heats: Determining $C_v, C_p, \gamma$ for different types of gases (monoatomic, diatomic, polyatomic) and using them in calculations.
- Conceptual Questions: Based on the Zeroth and Second Laws of Thermodynamics, entropy (though quantitative entropy is less common for JEE Main), and properties of different thermodynamic processes.
- Gas Laws and Equation of State: Often integrated with thermodynamic processes (e.g., $PV=nRT$).
Revision Checklist
- Thermodynamic Systems & Variables: Understand system types, state/path functions.
- First Law of Thermodynamics: $\Delta U = Q - W$ and its sign conventions.
- Work Done by Gas: Area under P-V curve, formulas for isothermal, isobaric processes.
- Internal Energy: $U = nC_vT$, degrees of freedom, $\gamma$ values.
- Molar Specific Heats: $C_p$, $C_v$, Mayer's Formula ($C_p - C_v = R$).
- All Thermodynamic Processes: P-V-T relations, $\Delta U$, $Q$, $W$ for Isothermal, Isobaric, Isochoric, Adiabatic processes.
- Cyclic Process: $Q_{net} = W_{net}$, $\Delta U = 0$.
- Second Law of Thermodynamics: Statements, implications.
- Heat Engines & Refrigerators: Efficiency, COP, Carnot cycle formulas ($T_L/T_H$).
- Conduction: Fourier's law, thermal resistance, series/parallel combinations.
- Convection: Newton's Law of Cooling (basic understanding).
- Radiation: Stefan-Boltzmann law, Emissivity, Net radiation, Wien's Displacement Law.
- Calorimetry: $Q = mc\Delta T$, $Q = mL$, principle of mixtures.
Last-Day Strategy for Thermodynamics & Heat Transfer
- Formula & Table Review: Go through the entire formula sheet, especially the table summarizing thermodynamic processes. Ensure you can recall each formula and its conditions of applicability.
- Sign Convention Drill: Mentally (or verbally) repeat the sign conventions for $Q$ and $W$ for different scenarios until it's second nature.
- P-V Diagram Interpretation: Briefly review how to interpret P-V diagrams for different processes and how to calculate work done from them.
- Special Values: Quickly recall $\gamma$ values for monoatomic, diatomic, polyatomic gases.
- Common Mistakes: Re-read the "Common Mistakes" section to reinforce awareness and avoid pitfalls during the exam.
- Quick Scan of Solved Examples: Look at the examples you've worked through or the ones provided here. Focus on the steps and the logic, not just the final answer. This helps in understanding application.
- No New Topics/Problems: Avoid starting new, complex problems or trying to learn new concepts. Focus solely on consolidating what you already know.
- Stay Calm: Confidence in fundamental formulas and concepts will help you approach problems systematically. Thermodynamics questions are often direct application; avoid overthinking.
By diligently following this resource and practicing consistently, you can master Thermodynamics and Heat Transfer and significantly boost your score in JEE Main Physics. Good luck!