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Chapter 3 from Moran and Shapiro

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It may exist in more than one phase, but the chemical composition ... Enthalpy in Two-Phase Region. H = U pV. h = u pv. h = (1-x)hf xhg = hf x(hg - hf) ... – PowerPoint PPT presentation

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Title: Chapter 3 from Moran and Shapiro


1
Properties ofPure Substances
2
Pure Substance
  • A substance that has a fixed (homogeneous and
    invariable) chemical composition throughout is
    called a pure substance.
  • It may exist in more than one phase, but the
    chemical composition is the same in all phases.

3
Pure Substance
  • Pure means of uniform and invariable chemical
    composition (but more than one molecular type is
    allowed). This allows air to be a pure
    substance.
  • All our substances will be pure. We will drop
    the use of the word. When we refer to a simple
    system we mean one filled with a pure
    substance--a simple, pure system.

4
Examples of Pure Substance
  • Water (solid, liquid, and vapor phases)
  • Mixture of liquid water and water vapor
  • Carbon Dioxide
  • Nitrogen
  • Homogeneous mixture of gases, such as air, as
    long as there is no change of phases.

5
Multiple phases mixture of a Pure Substance
Water
Air
vapor
vapor
liquid
liquid
Not pure, different condensation temperatures for
different components
Pure
6
Thermodynamic Properties
  • We have discussed extensive properties such as m,
    U, and V (for volume) which depend on the size or
    extent of a system, and
  • Intensive properties such as u, v, T, and P
    (sometimes we write a p for pressure, using P
    and p interchangeably) which are independent of
    system extent.

7
Important Questions ..
  • How many properties are needed to define the
    state of a system?
  • How do we obtain those properties?

Equation of State Property Tables
8
Review - State Postulate
  • The number of independent intensive properties
    needed to characterize the state of a system is
    n1 where n is the number of relevant
    quasiequilibrium work modes.
  • This is empirical, and is based on the
    experimental observation that there is one
    independent property for each way a systems
    energy can be independently varied.

9
Simple system
  • A simple system is defined as one for which only
    one quasiequilibrium work mode applies.
  • Simple compressible systems
  • Simple elastic systems
  • Simple magnetic systems
  • Simple electrostatic systems, etc.

10
Compressible
  • If we restrict our system to being compressible,
    we define what that quasiequilibrium work mode is

11
For a simple system,
  • We may write P P(v,T)
  • or v v(P,T)
  • or perhaps T T(P,v)

12
For a simple, pure substance
  • y0 y(y1,y2), or
  • P P(v,T), v v(P,T), and T T(P,v)
  • What do these equations define, in space?
  • Equations used to relate properties are called
    Equations of State

13
Equation of State
  • Any two independent, intrinsic properties are
    sufficient to fix the intensive state of a simple
    substance.
  • One of the major task of Thermodynamics is to
    develop the equations of state which relate
    properties at a give state of a substance.

14
Ideal gas law is a simple equation of state
Ru universal gas constant 8.3144
(kPa-m3)/(kgmol-K) 1.545 (ft-lbf)/(lbmol-R)
15
Phases of a Pure Substance
  • Solid phase -- molecules are arranged in a 3D
    pattern (lattice).
  • Liquid phase -- chunks of molecules float about
    each other, but maintain an orderly structure and
    relative positions within each chunk.
  • Gas phase -- random motion, high energy level.

16
Phase Equilibrium
p
p
p
p
p
vapor
liquid
liquid
vapor
liquid
ice
ice
heat
P 1 atm T 300 oC
P 1 atm T 0 oC
P 1 atm T 20 oC
P 1 atm T 100 oC
P 1 atm T -10 oC
17
Phase-change Process
  • Compressed liquid -- not about to evaporate
  • Saturated liquid -- about to evaporate
  • Saturated liquid-vapor mixture --two phase
  • Saturated Vapor -- about to condense
  • Superheated Vapor -- not about to condense

18
T-v Diagram
o
T, C
Isobaric process P 1 atm
300
5
Superheated vapor
2
3
Saturated mixture
100
4
Compressed liquid
20
1
v
19
P-T Diagram (Phase Diagram) of Pure Substances
20
Isothermal Process
Compressed Liquid
Superheated Vapor
21
Isobaric Process
Subcooled Liquid
a
Superheated Vapor
22
Water Expands on Freezing!
  • Ice floats on top of the water body (lakes,
    rivers, oceans, soft drinks, etc.).
  • If ice sinks to the bottom (contracts on
    freezing), the suns ray may never reach the
    bottom ice layers.
  • This will seriously disrupt marine life.

23
Saturation Temperature and Pressure
  • Tsat -- Temperature at which a phase change takes
    place at a given pressure.
  • Psat -- Pressure at which a phase change takes
    place at a given temperature.

24
Saturation Temperature
Tsat f (Psat) p 1atm 101.3
kPa, T 100 C p 500 kPa,
T 151.9 C
o
o
T and P are dependent during phase change Allow
us to control boiling temperature by
controlling the pressure (i.e., pressure cooker).
25
Latent Heat
  • Latent heat is the amount of energy absorbed or
    released during phase change
  • Latent heat of fusion -- melting/freezing
    333.7 kJ/kg for 1 atm H2O
  • Latent heat of vaporization --boiling/condensation
    2257.1 kJ/kg for 1
    atm H2O

26
P-v Diagram
P
Subcooled or compressed liquid region
Critical point
Superheated region --substance is 100 vapor
Two-phase or saturation region -- gas and liquid
coexist
Saturated liquid line
Saturated vapor line
v
27
P-v Diagram of a Pure Substance

SUPERHEATED
Isothermal process
v
28
T-v Diagram of a Pure Substance
v
29
Critical Supercritical
  • The state beyond which there is no distinct
    vaporization process is called the critical
    point.
  • At supercritical pressures, a substance gradually
    and uniformly expands from the liquid to vapor
    phase.
  • Above the critical point, the phase transition
    from liquid to vapor is no longer discrete.

30
Critical Point
  • Point at which the saturated vapor and saturated
    liquid lines coincide.
  • If T ? Tc or P ? Pc there is no clear
    distinction between the superheated vapor region
    and the compressed liquid region.

31
Critical Point
  • A point beyond which T ? Tc and a liquid-vapor
    transition is no longer possible at constant
    pressure. If T ? Tc , the substance cannot be
    liquefied, no matter how great the pressure.
  • Substances in this region are sometimes known as
    fluids rather than as vapors or liquids.

32
Vapor (Steam) Dome
  • The dome-shaped region encompassing the
    two-phase, vapor-liquid equilibrium region.
  • It is bordered by the saturated liquid line and
    the saturated vapor line, both of which end at
    the triple line and end at the critical point.
  • The region below the vapor dome is also called
    saturated liquid-vapor region, wet region,
    two-phase region, or saturation region.

33
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34
THERMODYNAMIC TABLES
35
STEAM IS NOT AN IDEAL GAS!
36
Steam Tables
  • Table A-1.1
  • Saturation water -- temperature table
  • Table A-1.2
  • Saturation water -- pressure table
  • Table A-1.3
  • Superheated vapor

37
For Water
P
Subcooled or compressed liquid region If
TTsat, p?psat If ppsat,T?Tsat
superheated region If TTsat , p?psat If ppsat
, TgtTsat
saturation region ppsat and TTsat
v
38
Two properties are not independent in the vapor
dome (the two-phase region)
  • The temperature and pressure are uniquely
    related. Knowing a T defines the P and vice
    versa.
  • Use quality to determine the state in two-phase
    region.

39
Quality is related to the horizontal differences
of P-v and T-v Diagrams

40
Quality
  • In a saturated liquid-vapor mixture, the mass
    fraction (not volume fraction) of the vapor phase
    is called the quality and is defined as
  • The quality may have values between 0 (saturated
    liquid) and 1 (saturated vapor). It has no
    meaning in the compressed liquid or superheated
    vapor regions.

41
What is v for something in the two-phase region?

v (1-x)vf xvg vf x(vg - vf)
vf xvfg
42
Enthalpy in Two-Phase Region
  • H U pV
  • h u pv

h (1-x)hf xhg hf x(hg - hf) hf
xhfg
43
Saturated Mixture
  • In the saturated mixture region, the average
    value of any intensive property y is determined
    fromwhere f stands for saturated liquid and
    g for saturated vapor.

44

Saturated Mixture

v vf x(vg - vf) vf xvfg u uf x(ug -
uf) uf xufg h hf x(hg - hf) hf
xhfg s sf x(sg - sf) sf xsfg
f saturated liquid g saturated vapor
45
Saturated Water (temperature)
46

Superheated Vapor
47
Examples 3-2 thru 3-7 Steam Tables A-1.1 and
A-1.3
48
TEAMPLAY
Complete the table below as a team. The
substance is water. Make sure everybody
understands how to do it!
P (MPa) T(?C) v(m3/kg) x (if appl.)
300 1.0
0.15 0.65
0.50 300
49
TEAMPLAY
Complete the table below as a team. The
substance is water. Use linear interpolation if
needed.
P(MPa) T(?C) u (kJ/kg) x (if appl.)
7.0 0.0
7.0 1.0
7.0 0.05
7.0 600
7.0 100
7.0 460
50
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