Chapter 3: The First Law of Thermodynamics
By the end of this section, you will be able to:
A thermodynamic system is any part of the universe whose thermodynamic properties are of interest.
Figure 3.2: (a) General system and surroundings. (b) Car engine as a system.
Figure 3.3: (a) Boiling tea kettle (open system). (b) Pressure cooker (closed system approximation).
Macroscopic Properties: We focus on average properties (pressure, volume, temperature) rather than individual molecular behaviors. - A system is typically assumed to be in equilibrium for simplified analysis.
Thermal Equilibrium: When two objects (or parts of a system) in thermal contact reach the same temperature, and there is no net heat transfer between them over time.
Zeroth Law of Thermodynamics:
If object 1 is in thermal equilibrium with objects 2 and 3, respectively, then objects 2 and 3 must also be in thermal equilibrium.
\[ \text{If } T_1 = T_2 \text{ and } T_1 = T_3, \text{ then } T_2 = T_3. \]
Note
This law fundamentally defines temperature: objects in thermal equilibrium have the same temperature.
To characterize a thermodynamic system, we use an equation of state:
A relationship between the basic measurable properties of the system (volume, pressure, temperature).
For a closed system, it’s symbolically written as: \[ f(p, V, T) = 0 \]
Tip
Example: For an ideal gas, the equation of state is \(pV - nRT = 0\), or \(pV = nRT\).
Variables:
By the end of this section, you will be able to:
Work is done when a force moves an object through a displacement. In thermodynamics, a system (like a gas) can do work by changing its volume against an external pressure.
Consider a gas in a cylinder with a movable piston:
The infinitesimal work done by the gas is: \[ dW = Fdx = pAdx \] Since \(dV = Adx\) (change in volume), this becomes: \[ dW = p dV \]
Figure 3.4: Work done by an expanding gas.
For a finite change in volume from \(V_1\) to \(V_2\), the net work is found by integration:
\[ W = \int_{V_1}^{V_2} p dV \]
Figure 3.5: Work done by gas expansion as the area under the pV curve.
The work done by a system depends on the specific thermodynamic path taken between initial and final states.
Figure 3.6: Three different paths (ABC, AC, ADC) between states A and C.
Notice \(W_{AC} \neq W_{ABC}\), showing path dependence.
The internal energy of a thermodynamic system is the sum of the mechanical energies of all its constituent molecules or entities.
\[ E_{int} = \sum_i (\overline{K_i} + \overline{U_i}) \]
For an ideal monatomic gas:
So, for \(n\) moles of an ideal monatomic gas: \[ E_{int} = n N_A \left(\frac{3}{2} k_B T\right) = \frac{3}{2} nRT \]
Important
The internal energy of an ideal monatomic gas depends only on temperature (\(T\)), not on pressure or volume.
By the end of this section, you will be able to:
The First Law of Thermodynamics is a statement of energy conservation for thermodynamic systems. It relates changes in internal energy to heat transfer and work done.
If \(Q\) is the heat exchanged between a system and its environment, and \(W\) is the work done by or on the system, the change in internal energy (\(\Delta E_{int}\)) of the system is:
\[ \Delta E_{int} = Q - W \]
Sign Conventions:
| Quantity | Description | Sign |
|---|---|---|
| \(Q > 0\) | Heat added to system | Positive |
| \(Q < 0\) | Heat removed from system | Negative |
| \(W > 0\) | Work done by system (expansion) | Positive |
| \(W < 0\) | Work done on system (compression) | Negative |
While \(Q\) and \(W\) are path-dependent, their difference (\(\Delta E_{int} = Q - W\)) is path-independent.
Figure 3.7: Different paths between states A and B.
Differential form of the First Law:
\[ dE_{int} = dQ - dW \] - For infinitesimal changes, where \(dE_{int}\) is the infinitesimal change in internal energy, \(dQ\) is infinitesimal heat exchanged, and \(dW\) is infinitesimal work done.
A system moves from state A to state B, receiving 400 J of heat and doing 100 J of work.
Change in internal energy (A to B):
\(\Delta E_{int, AB} = Q_{AB} - W_{AB} = 400 \text{ J} - 100 \text{ J} = 300 \text{ J}\).
Change in internal energy (B to A):
For a closed path, \(\Delta E_{int} = 0\). So, \(\Delta E_{int, AB} + \Delta E_{int, BA} = 0\).
\(\Delta E_{int, BA} = - \Delta E_{int, AB} = -300 \text{ J}\).
Heat absorbed along a different path (A to B):
If \(W'_{AB} = -400 \text{ J}\) (work done on the system) along a different path from A to B, \(\Delta E_{int, AB} = Q'_{AB} - W'_{AB}\)
\(300 \text{ J} = Q'_{AB} - (-400 \text{ J})\)
\(300 \text{ J} = Q'_{AB} + 400 \text{ J}\)
\(Q'_{AB} = -100 \text{ J}\). (Heat is removed from the system).
Note
Internal energy change is independent of the path. Heat and work depend on the path.
By the end of this section, you will be able to:
A thermodynamic process is the manner in which a system’s state changes from an initial state to a final state.
Quasi-static Process: - An idealized process where the change occurs infinitesimally slowly. - The system remains in thermodynamic equilibrium at every instant. - Macroscopic properties (P, V, T) are well-defined throughout the process. - Can be represented by a well-defined path on a state diagram (e.g., \(pV\) diagram).
Non-quasi-static Process: - Occurs rapidly, involving non-equilibrium intermediate states. - Macroscopic properties may not be well-defined during the process. - Cannot be represented by a defined path on a state diagram.
Figure 3.8: Quasi-static vs. non-quasi-static processes.
Several important types of quasi-static processes are defined by keeping one thermodynamic variable constant:
A cyclic process is one where the system returns to its initial state at the end of the process.
Note
Reversible Process: A process that can be made to retrace its path by differential changes in the environment. All reversible processes must be quasi-static. (Not all quasi-static processes are reversible, e.g., if friction is involved).
By the end of this section, you will be able to:
Consider an ideal gas in a fixed-volume vessel (isochoric process).
Therefore, for an ideal gas, the change in internal energy for any process is: \[ dE_{int} = nC_V dT \] This is because internal energy of an ideal gas depends only on temperature.
Consider an ideal gas in a vessel with a movable piston, under constant external pressure (isobaric process).
From the First Law (\(dE_{int} = dQ - dW\)):
\[ dE_{int} = nC_p dT - p dV \]
For an ideal gas, \(pV = nRT\). Differentiating with constant \(p\):
\(p dV = nR dT\).
Substitute this into the First Law:
\[ dE_{int} = nC_p dT - nR dT = n(C_p - R) dT \]
Since \(dE_{int}\) for an ideal gas is always \(nC_V dT\):
\[ nC_V dT = n(C_p - R) dT \]
This leads to the important relationship:
\[ C_p = C_V + R \] or \[ C_p - C_V = R \]
From the kinetic theory of gases, we found the molar heat capacity at constant volume to be: \[ C_V = \frac{d}{2}R \] where \(d\) is the number of degrees of freedom of a molecule.
Using \(C_p = C_V + R\): \[ C_p = \frac{d}{2}R + R = \left(\frac{d}{2} + 1\right)R \]
| Gas Type | Degrees of Freedom (\(d\)) | \(C_V\) | \(C_p\) | \(C_p - C_V\) |
|---|---|---|---|---|
| Monatomic | 3 (translational) | \(\frac{3}{2}R\) | \(\frac{5}{2}R\) | \(R\) |
| Diatomic | 5 (3 trans + 2 rot) | \(\frac{5}{2}R\) | \(\frac{7}{2}R\) | \(R\) |
| Polyatomic | 6 (3 trans + 3 rot) | \(3R\) (approx) | \(4R\) (approx) | \(R\) |
Note
Real Gases: Heat capacities of real gases are often slightly higher due to vibrational motion, especially at higher temperatures, but \(C_p - C_V\) remains close to \(R\).
By the end of this section, you will be able to:
In an adiabatic process, no heat is allowed to enter or leave the system (\(Q=0\)). - This occurs when the system is perfectly insulated or the process is very fast.
Consequences of Adiabatic Processes: - Compression: Work is done on the gas (\(W < 0\)), so \(\Delta E_{int} = -W > 0\). Internal energy increases, leading to a rise in temperature. - Expansion: Gas does work on the surroundings (\(W > 0\)), so \(\Delta E_{int} = -W < 0\). Internal energy decreases, leading to a drop in temperature.
Free Expansion of an Ideal Gas:
Figure 3.13: Free expansion of a gas.
For a quasi-static adiabatic process of an ideal gas, the following relationships hold:
\[ pV^\gamma = \text{constant} \] where \(\gamma\) is the adiabatic index or ratio of molar heat capacities: \[ \gamma = \frac{C_p}{C_V} \] Since \(C_p = C_V + R\), we know \(\gamma > 1\).
Other forms of the adiabatic condition: \[ TV^{\gamma-1} = \text{constant} \] \[ T^\gamma p^{1-\gamma} = \text{constant} \]
Tip
Example: For a monatomic ideal gas, \(C_V = \frac{3}{2}R\), \(C_p = \frac{5}{2}R\), so \(\gamma = \frac{5/2 R}{3/2 R} = \frac{5}{3} \approx 1.67\).
For a diatomic ideal gas, \(C_V = \frac{5}{2}R\), \(C_p = \frac{7}{2}R\), so \(\gamma = \frac{7/2 R}{5/2 R} = \frac{7}{5} = 1.40\).
Comparing paths on a \(pV\) diagram:
Figure 3.15: Adiabatic vs. isothermal expansions.
Since \(\gamma > 1\), the adiabatic curve is steeper than the isothermal curve at any given point. - This means for a given volume change, the pressure drops more steeply in an adiabatic expansion (due to temperature decrease) than in an isothermal expansion (where temperature is kept constant).
| Equation | Description |
|---|---|
| \(dW = p dV\) | Infinitesimal work done by a gas |
| \(W = \int_{V_1}^{V_2} p dV\) | Work done by a gas for a finite change in volume |
| \(E_{int} = \frac{3}{2} nRT\) | Internal energy of an ideal monatomic gas |
| \(\Delta E_{int} = Q - W\) | First Law of Thermodynamics |
| \(W = nRT \ln \left(\frac{V_2}{V_1}\right)\) | Work done in isothermal process (ideal gas) |
| \(dE_{int} = nC_V dT\) | Change in internal energy (ideal gas, any process) |
| \(C_p = C_V + R\) | Relation between molar heat capacities (ideal gas) |
| \(pV^\gamma = \text{constant}\) | Condition for quasi-static adiabatic process (ideal gas) |
| \(\gamma = \frac{C_p}{C_V}\) | Adiabatic index |
| Term | Definition |
|---|---|
| Thermodynamic System | Anything whose thermodynamic properties are of interest. |
| Surroundings | Everything outside the system that interacts with it. |
| Boundary | Imagined wall separating the system from its surroundings. |
| Isolated System | A system completely separated from its environment (no heat or matter exchange). |
| Closed System | A system that can exchange energy (heat, work) but not matter with its surroundings. |
| Open System | A system that can exchange both energy and matter with its surroundings. |
| Thermal Equilibrium | State where objects in thermal contact have the same temperature and no net heat transfer. |
| Zeroth Law of Thermodynamics | If objects A and B are each in thermal equilibrium with object C, then A and B are in thermal equilibrium with each other. |
| Equation of State | A mathematical relationship between a system’s measurable properties (e.g., \(f(p, V, T) = 0\)). |
| Extensive Variable | A property that depends on the amount of matter in the system (e.g., volume). |
| Intensive Variable | A property that is independent of the amount of matter in the system (e.g., temperature). |
| Internal Energy (\(E_{int}\)) | The sum of the mechanical energies of all molecules in a system. |
| First Law of Thermodynamics | States that the change in internal energy of a system equals the heat added to the system minus the work done by the system (\(\Delta E_{int} = Q - W\)). |
| State Function | A property whose value depends only on the current state of the system, not on the path taken to reach that state. |
| Thermodynamic Process | The manner in which a system’s state changes from an initial to a final state. |
| Quasi-static Process | An idealized process that occurs infinitesimally slowly, maintaining thermal equilibrium at each step. |
| Isothermal Process | A process in which the temperature of the system remains constant (\(\Delta T = 0\)). |
| Isobaric Process | A process in which the pressure of the system remains constant (\(\Delta p = 0\)). |
| Isochoric Process | A process in which the volume of the system remains constant (\(\Delta V = 0\)). |
| Adiabatic Process | A process in which no heat is exchanged between the system and its surroundings (\(Q = 0\)). |
| Cyclic Process | A process in which the system returns to its initial state (\(\Delta E_{int} = 0\)). |
| Molar Heat Capacity at Constant Volume (\(C_V\)) | Heat required to raise the temperature of 1 mole of gas by 1 K at constant volume. |
| Molar Heat Capacity at Constant Pressure (\(C_p\)) | Heat required to raise the temperature of 1 mole of gas by 1 K at constant pressure. |
| Adiabatic Index (\(\gamma\)) | The ratio of molar heat capacities, \(\gamma = C_p/C_V\). |