Properties of Pure Substances Study Notes
PROPERTIES OF PURE SUBSTANCES
First Law of Thermodynamics
Definition: Energy is conserved.
The total energy of an isolated system is constant; energy can be transformed from one form to another but cannot be created or destroyed.
First Law of Thermodynamics for a Closed System
Energy Change of a System, \Delta E{system} = E2 - E_1 = Q - W
Where:
\Delta E = change in energy
Q = heat added to the system
W = work done by the system
Energy Components:
\Delta KE + \Delta PE + \Delta U = Q - W
\Delta KE = change in kinetic energy
\Delta PE = change in potential energy
\Delta U = change in internal energy
Objectives
Introduce the concept of a pure substance.
Discuss the physics of phase-change processes.
Illustrate the P-v, T-v, and P-T property diagrams and P-v-T surfaces of pure substances.
Demonstrate the procedures for determining thermodynamic properties of pure substances from tables of property data.
Describe the hypothetical substance “ideal gas” and the ideal-gas equation of state.
Apply the ideal-gas equation of state in the solution of typical problems.
Introduce the compressibility factor, which accounts for the deviation of real gases from ideal-gas behavior.
Present some of the best-known equations of state.
3-1 Pure Substance
Definition: A substance that has a fixed chemical composition throughout.
Example: Air is a mixture of several gases, but it is considered to be a pure substance.
Figures:
Figure 3–1: Nitrogen and gaseous air are pure substances.
Figure 3–2: A mixture of liquid and gaseous water is a pure substance, but a mixture of liquid and gaseous air is not.
3-2 Phases of a Pure Substance
Molecular Behavior in Different Phases:
Solid Phase (Figure 3–3): Molecules are kept at fixed positions by strong intermolecular forces.
Liquid Phase (Figure 3–4): Molecules move around each other but are still in contact.
Gas Phase (Figure 3–4): Molecules move about randomly and are far apart.
3-3 Phase-Change Processes of Pure Substances
1. Compressed Liquid (Subcooled Liquid): A substance that is not about to vaporize.
Figure 3–5: At 1 atm and 20°C, water exists in the liquid phase (subcooled liquid).
2. Saturated Liquid: A liquid that is about to vaporize.
Figure 3–6: At 1 atm pressure and 100°C, water exists as a liquid that is about to vaporize (saturated liquid).
3. Saturated Liquid-Vapor Mixture: The state at which the liquid and vapor phases coexist in equilibrium.
Figure 3–7: As more heat is transferred, part of the saturated liquid vaporizes (saturated liquid-vapor mixture).
4. Saturated Vapor: A vapor that is about to condense.
Figure 3–8: At 1 atm pressure, the temperature remains constant at 100°C until the last drop of liquid is vaporized (saturated vapor).
5. Superheated Vapor: A vapor that is not about to condense (i.e., not a saturated vapor).
Figure 3–9: As more heat is transferred, the temperature of the vapor begins to rise (superheated vapor).
6. Reversibility of Phase Change: If the entire process between state 1 and state 5 is reversed by cooling the water while maintaining pressure, the heat released matches the heat added during the heating process.
Figure 3–10: T-v diagram for the heating process of water at constant pressure.
7. Saturation Temperature and Saturation Pressure:
Saturation Temperature: The temperature at which a pure substance changes phase at a given pressure.
Saturation Pressure: The pressure at which a pure substance changes phase at a given temperature.
Figure 3–11: Liquid-vapor saturation curve of a pure substance (numerical values are for water).
8. Saturation (Vapor) Pressure Table (Table 3–1) for Water at Various Temperatures:
\text{Temperature (°C)}
-10: P_{sat} = 0.260 kPa
-5: P_{sat} = 0.403 kPa
0: P_{sat} = 0.611 kPa
5: P_{sat} = 0.872 kPa
10: P_{sat} = 1.23 kPa
15: P_{sat} = 1.71 kPa
20: P_{sat} = 2.34 kPa
25: P_{sat} = 3.17 kPa
30: P_{sat} = 4.25 kPa
40: P_{sat} = 7.38 kPa
50: P_{sat} = 12.35 kPa
100: P_{sat} = 101.3 kPa (1 atm)
150: P_{sat} = 475.8 kPa
200: P_{sat} = 1554 kPa
250: P_{sat} = 3973 kPa
300: P_{sat} = 8581 kPa
3-4 Property Diagrams for Phase-Change Processes
Understanding Phase Changes: The variations of properties during phase change processes are studied with the help of property diagrams such as T-v, P-v, and P-T diagrams for pure substances.
Figure 3–15: T-v diagram of constant-pressure phase-change processes of a pure substance at various pressures (numerical values are for water).
Critical Point: The point at which the saturated liquid and saturated vapor states are identical.
Figure 3–16: At supercritical pressures, there is no distinct phase-change (boiling) process.
Regions on Property Diagrams:
Saturated Liquid Line
Saturated Vapor Line
Compressed Liquid Region
Saturated Liquid-Vapor Mixture Region (Wet Region)
Superheated Vapor Region
Figure 3–17: Property diagrams of a pure substance.
Pressure in Piston-Cylinder Device: The pressure can be reduced by decreasing the weight of the piston.
Figure 3–18 illustrates this concept.
Triple Point: The unique temperature and pressure at which a substance's solid, liquid, and vapor phases coexist in equilibrium.
Figure 3–20: At triple-point pressure and temperature, a substance exists in all three phases in equilibrium.
T{tp} = 0.01 °C, P{tp} = 0.6117 kPa
Sublimation: The process of passing from the solid phase directly into the vapor phase.
Figure 3–21: At low pressures (below the triple-point value), solids evaporate without melting first.
3-5 Property Tables
Purpose of Property Tables: Relationships among thermodynamic properties are complex; therefore, properties are often presented in table form.
Measurable vs. Calculable Properties: Some thermodynamic properties can be measured easily, while others are calculated using relationships between them and measurable properties.
Results are presented in tables in a convenient format.
Saturated Liquid and Saturated Vapor States:
Figure 3–27: Depicts a partial list from Table A–4 detailing saturation properties of water.
Definitions:
v_f = specific volume of saturated liquid
v_g = specific volume of saturated vapor
v{fg} = vg - v_f
Examples
Example Questions:
If T{sat} = 30°C → Determine P? , vf?
If T{sat} = 100°C → Determine P? , vg?
If P{sat} = 1.0 kPa → Determine T? , vf?
If P{sat} = 10.0 kPa → Determine T? , vg?
Example Problems
EXAMPLE 3-1: Pressure of Saturated Liquid in a Tank
A rigid tank contains 50 kg of saturated liquid water at 90°C.
Determine:
Saturation Pressure:
P_{sat} = 70.183 kPa
Volume of Tank:
V = (50 kg) imes (0.001036 m³/kg) = 0.0518 m³ → 51.8 L
EXAMPLE 3-2: Temperature of Saturated Vapor in a Cylinder
A piston-cylinder device contains 2 ft³ of saturated water vapor at 50 psia pressure.
Determine: Temperature and mass of vapor inside the cylinder using English unit tables.