Notes
Slide Show
Outline
1
Thermodynamics I
  • Asst.Prof.Dr.Denpong Soodphakdee
  • Department of Mechanical Engineering
2
Pure Substance
  • Fixed chemical composition throughout
  • There are three phases
    • Solid
    • Liquid
    • Gas
  • Phase can be changed from one to another.
3
Phase-Change Processes of Pure Substances
  • Compressed Liquid :- not about to vaporize
  • Saturated Liquid :- about to vaporize
  • Saturated Vapor :- about to condense
  • Saturated Liquid-Vapor Mixture :- liquid and vapor phases coexist
  • Superheated vapor :- not about to condense
4
Phase-Change Processes of Pure Substances
  • T-v diagram for the heating process of water at constant pressure.
5
Property Diagrams for Phase-Change Processes
  • Critical point (the point at which the saturated liquid and saturated vapor states are identical)
  • Saturated liquid line
  • Saturated vapor line
  • Compressed liquid region
  • Superheated vapor region
  • Saturated liquid-vapor mixture region or wet region
6
Property Diagrams for Phase-Change Processes :: T-v Diagram
7
Property Diagrams for Phase-Change Processes :: P-v Diagram
8
Property Diagrams for Phase-Change Processes :: P-v Diagram
9
Property Diagrams for Phase-Change Processes :: P-v Diagram
10
Property Diagrams for Phase-Change Processes :: P-T Diagram
11
Property Diagrams for Phase-Change Processes :: P-v-T Surface
12
Property Diagrams for Phase-Change Processes :: P-v-T Surface
13
Enthalpy
  • Enthalpy is a combination property



  • Enthalpy per unit mass
14
Saturated Liquid and Saturated Vapor States
15
Saturated Liquid and Saturated Vapor States
16
Example
  • A mass of 200 gm of saturated liquid water is completely vaporized at a constant pressure of 100 kPa. Determine the volume change of the water.
17
Saturated Liquid-Vapor Mixture
  • To analyze the mixture of saturated liquid and saturated vapor, the proportions of the liquid and vapor phases in the mixture needs to be known.
18
Saturated Liquid-Vapor Mixture
  • Saturated Liquid-Vapor Mixture
19
Saturated Liquid-Vapor Mixture
  • Average value of specific volume and quality
20
Saturated Liquid-Vapor Mixture
  • Average of internal energy, enthalpy and other properties
21
Example
  • A rigid tank contains 10 kg of water at 90 °C. If 8 kg of the water is in the liquid form and the rest is in the vapor form, determine
    (a) the pressure in the tank and
    (b) the volume of the tank.


22
Example
  • An 80-L vessel contains 4 kg of refrigerant-12 at a pressure of 160 kPa. Determine
    (a) the temperature of the refrigerant,
    (b) the quality,
    (c) the enthalpy of the refrigerant, and
    (d) the volume occupied by the vapor phase.
23
Superheated Vapor
  • Lower pressures
    (P < Psat at a given T)
  • Higher temperatures
    (T > Tsat at a given P)
  • Higher specific volumes
    (v > vg at a given P or T)
  • Higher internal energies
    (u > ug at a given P or T)
  • Higher enthalpies
    (h > hg at a given P or T)
24
Example
  • Determine the temperature of water at a state of P = 0.5 MPa and h = 2890 kJ/kg.
25
Compressed Liquid
  • Variation of properties in compressed liquid with pressure is very mild.
  • A general approximation is to treat compressed liquid as saturated liquid at the given temperature.
26
Compressed Liquid
  • Higher pressures (P > Psat at a given T)
  • Lower temperatures (T < Tsat at a given P)
  • Lower specific volumes (v < vg at a given P or T)
  • Lower internal energies (u < ug at a given P or T)
  • Lower enthalpies (h < hg at a given P or T)
27
Example
  • Determine the internal energy of compressed liquid water at 80°C and 5 MPa, using
    (a) data from the compressed liquid table and
    (b) saturated liquid data. What is the error involved in the second case?
28
Reference State and Reference Values
  • The value of u, h, and s can not be measured directly.
  • They are calculated relatively between thermodynamic properties, not the value at that state.
  • Reference state will give the reference value of zero.
  • Example reference state:
    • Water : saturated liquid at 0.01°C
    • R134a : saturated liquid at -40°C
29
The Ideal-Gas Equation of State
  • Any equation that relates the pressure, temperature, and specific volume of a substance is call an equation of state.
  • Property relations that involves other properties of a substance at equilibrium state are also called equation of state.
30
The Ideal-Gas Equation of State
  • The vapor phase of a substance is call a gas when it is above the critical temperature.
  • Vapor usually implies a gas that is not far from a state of condensation.
  • At low pressures the volume of a gas is proportional to its temperature.
31
The Ideal-Gas Equation of State
  • The gas constant R is determine from
32
Example
  • Determine the mass of the air in a room whose dimension are 4m´5m´6m at 100 kPa and 25°C.


33
Compressibility Factor
A Measure of Deviation from Ideal-Gas Behavior
34
Compressibility Factor
A Measure of Deviation from Ideal-Gas Behavior
  • The deviation from ideal-gas behavior at a given temperature and pressure can accurately be accounted for by a correction factor called compressibility factor, Z.
35
Compressibility Factor
A Measure of Deviation from Ideal-Gas Behavior
36
Engineering Equation Solver
  • EES ('ease') is a revolutionary program which will change the way you think and work.
  • EES provides capabilities not found in any other equation solving program.
  • EES will solve large sets of non-linear algebraic and differential equations.
  • EES also provides publication-quality plots, linear and non-linear regression, optimization, unit conversion and consistency checking, and uncertainty analyses.
  • Built-in functions are provided for thermodynamic and transport properties of many substances, including steam, air, refrigerants, cryogenic fluids, JANAF table gases, hydrocarbons and psychrometrics.
37
Engineering Equation Solver