Title: Chapter 3 from Moran and Shapiro
1Properties ofPure Substances
2Pure 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.
3Pure 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.
4Examples 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.
5Multiple phases mixture of a Pure Substance
Water
Air
vapor
vapor
liquid
liquid
Not pure, different condensation temperatures for
different components
Pure
6Thermodynamic 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.
7Important Questions ..
- How many properties are needed to define the
state of a system? - How do we obtain those properties?
Equation of State Property Tables
8Review - 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.
9Simple 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.
10Compressible
- If we restrict our system to being compressible,
we define what that quasiequilibrium work mode is
11For a simple system,
- We may write P P(v,T)
- or v v(P,T)
- or perhaps T T(P,v)
12For 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
13Equation 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.
14Ideal gas law is a simple equation of state
Ru universal gas constant 8.3144
(kPa-m3)/(kgmol-K) 1.545 (ft-lbf)/(lbmol-R)
15Phases 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.
16Phase 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
17Phase-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
18T-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
19P-T Diagram (Phase Diagram) of Pure Substances
20Isothermal Process
Compressed Liquid
Superheated Vapor
21Isobaric Process
Subcooled Liquid
a
Superheated Vapor
22Water 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.
23Saturation 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.
24Saturation 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).
25Latent 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
26P-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
27P-v Diagram of a Pure Substance
SUPERHEATED
Isothermal process
v
28T-v Diagram of a Pure Substance
v
29Critical 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.
30Critical 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.
31Critical 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.
32Vapor (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.
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34THERMODYNAMIC TABLES
35STEAM IS NOT AN IDEAL GAS!
36Steam Tables
- Table A-1.1
- Saturation water -- temperature table
- Table A-1.2
- Saturation water -- pressure table
- Table A-1.3
- Superheated vapor
37For 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
38Two 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.
39Quality is related to the horizontal differences
of P-v and T-v Diagrams
40Quality
- 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.
41What is v for something in the two-phase region?
v (1-x)vf xvg vf x(vg - vf)
vf xvfg
42Enthalpy in Two-Phase Region
h (1-x)hf xhg hf x(hg - hf) hf
xhfg
43Saturated 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
45Saturated Water (temperature)
46 Superheated Vapor
47Examples 3-2 thru 3-7 Steam Tables A-1.1 and
A-1.3
48TEAMPLAY
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
49TEAMPLAY
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
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