Pure substances are the building blocks of thermodynamics. They have unique properties that change with and . Understanding these properties is crucial for analyzing energy systems and processes in engineering applications.
Phase diagrams and property tables are essential tools for thermodynamicists. They help visualize and quantify how substances behave under different conditions. Mastering these tools allows engineers to predict and optimize the performance of various thermal systems.
Phase diagrams and property tables
Phase diagram features
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A is a graphical representation of the equilibrium states of a pure substance, showing pressure on the vertical axis and temperature on the horizontal axis
Key features of a phase diagram include:
: The point where all three phases (solid, liquid, and ) coexist in equilibrium (water triple point: 0.01°C and 0.6 kPa)
: The point where the distinction between liquid and gas phases disappears (water critical point: 374°C and 22.1 MPa)
: Represents the equilibrium between solid and gas phases (dry ice at atmospheric pressure)
: Represents the equilibrium between solid and liquid phases (water freezing at 0°C and 1 atm)
: Represents the equilibrium between liquid and gas phases (water boiling at 100°C and 1 atm)
Property tables and interpolation
Property tables provide thermodynamic data for pure substances at various temperatures and pressures
Properties listed in the tables include , , , and
and saturated vapor states are represented in property tables (water at 100°C and 1 atm)
and compressed liquid regions are also included in the tables (steam at 200°C and 1 atm)
Interpolation may be necessary to determine properties at conditions not explicitly listed in the tables
Linear interpolation is used for most properties (specific volume, internal energy, enthalpy)
Logarithmic interpolation is used for entropy due to its logarithmic nature
Using phase diagrams and property tables together
Phase diagrams and property tables can be used together to determine the state and properties of a pure substance at a given temperature and pressure
Locate the given temperature and pressure on the phase diagram to identify the state (solid, liquid, gas, or )
Use the property tables to find the corresponding thermodynamic properties for the identified state
If the state is a two-phase mixture, use and the properties of the saturated liquid and saturated vapor to calculate the mixture properties (water at 50°C and 1 atm)
Thermodynamic property calculations
Steam tables
Steam tables provide thermodynamic properties of water and steam at various temperatures and pressures
Properties listed in steam tables include specific volume, internal energy, enthalpy, and entropy
Saturated water and saturated steam properties are listed (water at 100°C and 1 atm)
Superheated steam and compressed water regions are also included in the tables (steam at 200°C and 1 atm)
Interpolation may be necessary to determine properties at conditions not explicitly listed in the tables
Linear interpolation is used for most properties (specific volume, internal energy, enthalpy)
Logarithmic interpolation is used for entropy due to its logarithmic nature
Refrigerant charts
Refrigerant charts provide thermodynamic properties for common refrigerants at various temperatures and pressures
Properties listed in refrigerant charts are similar to those in steam tables (specific volume, internal energy, enthalpy, and entropy)
Refrigerant charts are used to determine properties of refrigerants in vapor compression refrigeration cycles (R-134a in a household refrigerator)
Calculating properties using tables and charts
To calculate thermodynamic properties using steam tables or refrigerant charts, locate the appropriate table or chart based on the given temperature and pressure conditions
If the given conditions match a table entry exactly, the properties can be read directly from the table
If the given conditions fall between table entries, interpolation is required to estimate the properties
Use linear interpolation for most properties (specific volume, internal energy, enthalpy)
Use logarithmic interpolation for entropy due to its logarithmic nature
Pure substance phase changes
Types of phase changes
Phase changes occur when a pure substance transitions between solid, liquid, and gas phases due to changes in temperature or pressure
Melting (solid to liquid) and freezing (liquid to solid) occur at the fusion curve on a phase diagram (ice melting at 0°C and 1 atm)
Vaporization (liquid to gas) and (gas to liquid) occur at the vaporization curve on a phase diagram (water boiling at 100°C and 1 atm)
Boiling is a specific type of vaporization that occurs at the saturation temperature corresponding to the given pressure
Sublimation (solid to gas) and deposition (gas to solid) occur at the sublimation curve on a phase diagram (dry ice sublimating at -78°C and 1 atm)
Behavior during phase changes
During a phase change, the temperature of a pure substance remains constant as heat is added or removed
The specific volume and other properties may change significantly during a phase change
Specific volume increases during melting and vaporization (water expanding when frozen)
Specific volume decreases during freezing and condensation (steam condensing to a smaller volume)
The , vaporization, or sublimation is the amount of energy required to change the phase of a unit mass of a pure substance at a constant temperature and pressure
Latent heat of fusion for water: 333.55 kJ/kg at 0°C and 1 atm
for water: 2257 kJ/kg at 100°C and 1 atm
Two-phase mixture properties
Quality and the lever rule
A two-phase mixture is a system in which two phases of a pure substance coexist in equilibrium (liquid-vapor mixture in a steam power plant)
Quality (x) is the mass fraction of vapor in a two-phase mixture, ranging from 0 (saturated liquid) to 1 (saturated vapor)
Quality can be calculated using the lever rule:
x=(v−vf)/(vg−vf)
where v is the specific volume of the mixture, vf is the specific volume of saturated liquid, and vg is the specific volume of saturated vapor
Calculating mixture properties
The specific volume of a two-phase mixture can be determined using the quality and the specific volumes of the saturated liquid and saturated vapor
v=(1−x)⋅vf+x⋅vg
where v is the specific volume of the mixture, x is the quality, vf is the specific volume of saturated liquid, and vg is the specific volume of saturated vapor
Other thermodynamic properties of a two-phase mixture, such as internal energy, enthalpy, and entropy, can be calculated using quality and the respective properties of the saturated liquid and saturated vapor
u=(1−x)⋅uf+x⋅ug (internal energy)
h=(1−x)⋅hf+x⋅hg (enthalpy)
s=(1−x)⋅sf+x⋅sg (entropy)
Example: A two-phase mixture of water at 100°C and 1 atm with a quality of 0.5 has a specific volume of 0.8263 m³/kg, internal energy of 1443.5 kJ/kg, enthalpy of 1675.4 kJ/kg, and entropy of 4.1758 kJ/(kg·K)