Uploaded by Tanmay Mishra

2 Pure Substance

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THERMODYNAMICS
Course no. ME22002
Section 1
Dr. Sourav Mitra
Room No. 204 (first floor)
Department of Mechanical Engineering
1
THERMODYNAMICS:
Properties of Pure
substance
2
T-v diagram for isobaric heating of water
3
T-v chart for water
4
T-v chart for water
Isobars
4
T-v chart for water
Isobars
Isotherms
4
T-v chart for water
Isobars
Isotherms
4
T-v chart for water
5
T-v chart for water
As we increase
pressure the twophase region shortens
5
T-v chart for water
As we increase
pressure the twophase region shortens
5
Critical point
6
Critical point
The point at which the saturated
liquid and saturated vapor states are
identical
6
Critical point
The point at which the saturated
liquid and saturated vapor states are
identical
The corresponding temperature is
called critical temperature and
pressure is called critical pressure.
6
P-v chart for water
7
P-v chart for water
Isobars
7
P-v chart for water
Isobars
7
P-T chart for water
8
P-T chart including solid phase
9
P-T chart including solid phase
A-B: Melting/freezing
A
B
9
P-T chart including solid phase
A-B: Melting/freezing
A
B
C
C-D: Boiling/condensation
D
9
P-T chart including solid phase
A-B: Melting/freezing
B
A
C
C-D: Boiling/condensation
D
E-F: Sublimation/deposition
E
F
9
P-v-T chart for water
10
P-v-T chart for water
10
P-v-T chart for water
10
P-v-T chart for substance that contract on
freezing
11
P-v-T chart for substance that contract on
freezing
11
P-v-T chart for substance that contract on
freezing
11
Application of triple point
Ptr & Ttr are fixed for a pure substance
12
Application of triple point
Ptr & Ttr are fixed for a pure substance
The cell is filled with pure deionized
water and then evacuated. The top
portion is not air but water vapor
12
Application of triple point
Ptr & Ttr are fixed for a pure substance
Vapor
Liquid
Cool using dry ice
Ice
The cell is filled with pure deionized
water and then evacuated. The top
portion is not air but water vapor
611.73 Pa
0.01°C
Can be used for calibration of
sensors
12
Application of triple point
Ptr & Ttr are fixed for a pure substance
Vapor
Liquid
Cool using dry ice
Ice
The cell is filled with pure deionized
water and then evacuated. The top
portion is not air but water vapor
611.73 Pa
0.01°C
Can be used for calibration of
sensors
If you achieve 3 phases simultaneously, then Ptr , Ttr is obtained.
12
Application of triple point
Ptr & Ttr are fixed for a pure substance
Vapor
Liquid
Cool using dry ice
Ice
The cell is filled with pure deionized
water and then evacuated. The top
portion is not air but water vapor
611.73 Pa
0.01°C
Can be used for calibration of
sensors
If you achieve 3 phases simultaneously, then Ptr , Ttr is obtained.
What is the problem in using freezing point and boiling point of water?
12
Significance of critical point
Pcr
Tcr
13
Significance of critical point
Suppose you are in vapor region with
T<Tcr
One can liquefy the vapor by the
action of pressure alone
Pcr
Tcr
13
Significance of critical point
Suppose you are in vapor region with
T<Tcr
One can liquefy the vapor by the
action of pressure alone
Pcr
Suppose you are in vapor region
with T>Tcr
Liquefaction of the vapor by the
action of pressure alone is
impossible !!
Tcr
13
Significance of critical point
Suppose you are in vapor region with
T<Tcr
One can liquefy the vapor by the
action of pressure alone
Pcr
Suppose you are in vapor region
with T>Tcr
Liquefaction of the vapor by the
action of pressure alone is
impossible !!
Tcr
Critical temp: the temperature beyond which vapor cannot be
liquefied by the action of pressure alone
13
Significance of critical point
Pcr
Tcr
14
Significance of critical point
Suppose you are in vapor region with
P<Pcr
One can liquefy the vapor by the
action of temperature alone
Pcr
Tcr
14
Significance of critical point
Suppose you are in vapor region with
P<Pcr
One can liquefy the vapor by the
action of temperature alone
Pcr
Suppose you are in vapor region
with P>Pcr
Liquefaction of the vapor by the
action of temperature alone is
impossible !!
Tcr
14
Significance of critical point
Suppose you are in vapor region with
P<Pcr
One can liquefy the vapor by the
action of temperature alone
Pcr
Suppose you are in vapor region
with P>Pcr
Liquefaction of the vapor by the
action of temperature alone is
impossible !!
Tcr
Critical temp: the pressure beyond which vapor cannot be liquefied by
the action of temperature alone
14
Significance of critical point
Supercritical fluid
Pcr
Tcr
15
Significance of critical point
Supercritical fluid
Pcr
Tcr
Fluid with temperature greater than critical temperature and pressure
higher than critical pressure is called “Supercritical Fluid”
15
Quality or dryness fraction of vapor
16
Quality or dryness fraction of vapor
16
Quality or dryness fraction of vapor
x
vg
v
16
Quality or dryness fraction of vapor
 v  1  x  v f  xvg
x
vg
v
Mixture specific volume: v
16
Quality or dryness fraction of vapor
vapor fraction within the
saturated mixture
17
Quality or dryness fraction of vapor
vapor fraction within the
saturated mixture
Saturated vapor: x = 1
Saturated liquid: x = 0
17
Quality or dryness fraction of vapor
vapor fraction within the
saturated mixture
Quality is an intensive property
Saturated vapor: x = 1
Saturated liquid: x = 0
17
Quality or dryness fraction of vapor
vapor fraction within the
saturated mixture
Saturated vapor: x = 1
Saturated liquid: x = 0
Quality is an intensive property
Can be used with other independent
intensive property like P or T for
defining state of saturated mixture
17
Quality or dryness fraction of vapor
vapor fraction within the
saturated mixture
Saturated vapor: x = 1
Saturated liquid: x = 0
Quality is an intensive property
Can be used with other independent
intensive property like P or T for
defining state of saturated mixture
Are x and v independent intensive properties ?
17
Ideal and Real gas
18
Ideal and Real gas
Ideal gas assumption: Molecules are far apart hence no intermolecular forces
18
Ideal and Real gas
Ideal gas assumption: Molecules are far apart hence no intermolecular forces
Low density gases
18
Ideal and Real gas
Ideal gas assumption: Molecules are far apart hence no intermolecular forces
Low density gases
•
•
But what constitutes low density?
By how much does an actual gas at a given pressure and
temperature deviate from ideal-gas behavior?
18
Ideal and Real gas
Ideal gas assumption: Molecules are far apart hence no intermolecular forces
Low density gases
•
•
But what constitutes low density?
By how much does an actual gas at a given pressure and
temperature deviate from ideal-gas behavior?
Error between ideal gas and
experimental measurements
for
saturated
and
superheated water vapor
18
Ideal and Real gas
Ideal gas assumption: Molecules are far apart hence no intermolecular forces
Low density gases
•
•
But what constitutes low density?
By how much does an actual gas at a given pressure and
temperature deviate from ideal-gas behavior?
Error between ideal gas and
experimental measurements
for
saturated
and
superheated water vapor
High temperatures
or very low pressure
18
Compressibility factor
P0
Reduced pressure: PR = P/Pcr
Reduced temperature: TR = T/Tcr
19
Compressibility factor
•
Bring in a factor called
“compressibility factor”
to define the deviation:
Pv/RT=Z
P0
Reduced pressure: PR = P/Pcr
Reduced temperature: TR = T/Tcr
19
Compressibility factor
•
Bring in a factor called
“compressibility factor”
to define the deviation:
Pv/RT=Z
•
•
Z=1 (ideal gas)
Any value of Z (real gas)
P0
Reduced pressure: PR = P/Pcr
Reduced temperature: TR = T/Tcr
19
Compressibility factor
•
Bring in a factor called
“compressibility factor”
to define the deviation:
Pv/RT=Z
•
•
Z=1 (ideal gas)
Any value of Z (real gas)
P0
vreal = ZRT/P
videal = RT/P
So Z = vreal/videal
Reduced pressure: PR = P/Pcr
Reduced temperature: TR = T/Tcr
19
Compressibility factor
•
Bring in a factor called
“compressibility factor”
to define the deviation:
Pv/RT=Z
•
•
Z=1 (ideal gas)
Any value of Z (real gas)
P0
vreal = ZRT/P
videal = RT/P
So Z = vreal/videal
•
•
•
Z=1 (no Inter-Molecular force)
Z<1 (attractive forces)
Z>1 (repulsive forces)
Reduced pressure: PR = P/Pcr
Reduced temperature: TR = T/Tcr
19
Compressibility factor
Compressibility
factor for nitrogen
•
•
•
Z=1 (no Inter-Molecular force)
Z<1 (attractive forces)
Z>1 (repulsive forces)
20
Property tables and charts
P-h chart of steam
Steam table
We don’t need these charts and tables
Use electronic tool to obtain this database
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