ap3290_chapter_5_ii_2009
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2.3. Cooling by isentropic expansion (adiabatic expansion) process:
S P
T
∂
∂
It has been pointed out earlier that thermodynamic processes can be mathematically
described by a partial derivative under specific conditions.
“isentropic” above indicates no change of entropy ( 0=dS , i.e. 0=dQ ) happened in
the process. “isentropic” process is equivalent to “adiabatic” process (since 0=dS means
0=dQ ).
“expansion” means when volume expands and pressure will change accordingly.
“cooling” means the temperature decreases.
Therefore, cooling by isentropic expansion is dealing with the T~P relationship, or is
aking how temperature changes with respect to the decrease of pressure (when volume
expands) under the isentropic condition?
Thus, the study of “cooling by isentropic expansion” is to answer the following
questions: ?=
∂
∂
S P
T
How does the temperature of a gas change when it expands?
Derivation ofS P
T
∂
∂
:
Entropy S is a state function, for ),( PT S , mathematically we have
),(TP
dPP
S dT
T
S PT dS
∂
∂+
∂
∂=
For isentropic process (constant entropy process), 0=dS :
dPP
S dT
T
S
TP
0
∂
∂+
∂
∂=∴
thus
P
T
∂
∂
∂
∂
−=
∂
∂
T
S
P
S
P
T
S
Eq5-6
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*Or Eq5-6 can also be obtained directly by applying the “triple product rule”:
For ),( PT S :
1−=
∂
∂
∂
∂
∂
∂
S T P P
T
S
P
T
S
Therefore:
P
T
T P
S
T
S
P
S
S
P
T
S P
T
∂
∂
∂
∂
−=
∂
∂
∂
∂−=
∂
∂ 1
--------------------------------------------------------------------------------------------
Applying the Maxwell’s relation (from VdPSdT dG +−= ):
PT
-
∂
∂=
∂
∂
T V
PS ,
Since the volume expansion coefficient:
P
1
∂
∂=
T
V
V α , or V
T
V
P
α =
∂
∂. The specific heat
P
∂
∂=
T
S T C P , or T C
T
S P /
P
=
∂
∂is the,
Therefore Eqn5-6 becomes:
0
P
T>=
∂
∂
∂∂
−=
∂
∂
PS C
TV
T
S
PS
P
T α Eq5-7
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Positive slope means that when pressure P decreases (volume expands), temperature T will
drop. It can be concluded that isentropic expansion always causes a decrease in temperature.
This process can be used for gas cooling.
2.4.
Joule-Thomson effect(Throttling process): Cooling by isenthalpic expansion
H P
T
∂
∂
Let us perform a thermodynamic process: a high-pressure gas is forced through a
constriction, such as a partially opened valve (a throttle) or a porous wall. The throttle valve
is well thermally insulated so that no heat is transferred during the process.
The gas initially has a pressure P1, temperature T1 and volume V1. After it passes
through the valve, its final pressure is P2 and the volume is V2
The first law for this system can be written as: W QU U U +=−=∆12
Since the system is thermally insulated, Q=0, so W U U =− 12 ,
2211
0
2
0
121
2
1
V PV PdV PdV PW W W V
V
−=−−=+= ∫∫
so we obtain:
221112 V PV PU U −=− , i.e., 111222 V PU V PU +=+ ,
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Since the enthalpy is defined as PV U H += , so we get
0or1212
=−=∆= H H H H H
Thus throttling process is a constant enthalpy process (isenthalpic process).
Given a particular gas and the initial conditions P1 and T1, and final pressure P2 , we
wish to know what the final temperature T2 will be. In other words, we want to know the
change of temperature of the gas (from T1 to T2) with respect to the change of its pressure
(from P1 to P2) in this isenthalpic process:
?=
∂
∂=
H
JT P
T µ Eqn5-8
This thermodynamic quantity µJT is known as the Joule-Thomson coefficient, which is named
after James Joule and William Thomson, who together studied this process in the 1850s.
To find out
H
JT P
T
∂
∂= µ , we proceed by starting from the relationship:
dPV P
S T dT
T
S T VdPdP
P
S dT
T
S T dH
T PT P
+
∂
∂+
∂
∂=+
∂
∂+
∂
∂=∴
Applying the Maxwell’s relation:PT T
V
P
S
∂
∂=
∂
∂- , and
P
PP
S T C
∂
∂= ,
dH becomes:
dP
T
V T V dT C dH
P
P
∂
∂−+=
For isenthalpic process (constant enthalpy process): 0=dH , so
dPV T
V T dT C
P
P
−
∂
∂=
therefore we obtain the expression for the Joule-Thomson coefficient:
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−
∂
∂=
∂
∂= V
T
V T
C P
T
PP H
JT
1 µ Eqn5-10
For an ideal gas, ,,T
V
P
nR
T
V nRT PV
P
==
∂
∂→= , it is straightforward to show that
0= JT
µ , the temperature of an ideal gas does not change after throttling expansion.
However, when a real gas expands freely at constant enthalpy, the final temperature
( 2T ) may either decrease or increase, depending on the initial temperature ( 1T ) and
pressure( 1P ). For any given pressure, a real gas has a Joule-Thomson (Kelvin) inversion
temperature InvT . (i) When initial temperature of the gas InvT T >1 , throttling expansion
causes the temperature to rise ( 12 T T >
). (ii) When InvT T <
1 isenthalpic expansion causes
cooling ( 12 T T < ).
For most gases at atmospheric pressure, the inversion temperature InvT is fairly high
(above room temperature), and so isenthalpic expansion can be applied for gas cooling at
those temperature and pressure conditions.
The value of µ JT , representing the change of temperature with respect to a change of pressure,
depends on the specific gas, as well as the initial temperature and pressure of the gas before
expansion. For all real gases, µ JT will equal zero at some temperature point called the Joule-
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Thomson inversion temperature or inversion point. It is the temperature where the
coefficient changes sign (i.e., where the coefficient equals zero).
In any gas expansion, the gas pressure decreases, meaning P∂ is always negative
( 0<∂P ). With that in mind ( P
T JT
∂
∂
= µ ),the following table explains when the Joule-
Thomson effect cools or heats a real gas.
If the gas temperature is then µ JT is since P∂ is thus T ∂ must be so the gas
below the inversion temperature >0 always “-“ negative cools
above the inversion temperature <0 always “-“ positive heats
Helium and hydrogen are two gases whose Joule-Thomson inversion temperatures at
one atmosphere are very low (e.g., about −222 °C for helium). Thus, helium and hydrogen
will warm when expanded at constant enthalpy at typical room temperatures. So hydrogen
expansion at room temperature is very dangerous.
3. Gas cooling, liquefaction, and low temperature achievement
The Joule-Thomson effect is applied in the Linde technique as a standard process in
the petrochemical industry, where the cooling effect is used to liquefy gases (for the
production of liquid O2, N2, H2, and He), so that extremely low temperature can be achieved.
From air liquefaction to air separation: with air liquefaction, German engineer Carl
von Linde(1891–1934), created the conditions needed to produce pure gases using low-
temperature processes. These gases include not only oxygen and nitrogen, but also hydrogen
and inert gases - a technology for which the future has only just begun.
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Sketch of the first air liquefaction plant from 1895.
A gas must be below its inversion temperature to be cooled and liquefied. Once a gas has
been pre-cooled to a temperature lower than the maximum inversion temperature, the
optimum pressure, from which to start throttling, corresponds to a point on the inversion
curve, where the Joule-Thomson coefficient 0= JT
µ . Starting at this pressure and ending at
a lower pressure (after expansion), the process produces a large temperature drop.
Consequently, the gas that has been cooled by throttling is used to cool the incoming gas,
which after throttling becomes still cooler. After successive cooling processes, the
temperature of the gas is lowered to such a temperature that , after throttling, it becomes
partly liquefied.
Gas Inversion temperature TInv Liquefying temperature TLiq
At 1atm
O2 620oC -183
oC
N2 352oC -196oC
H2 -71oC -253oC
Ne -239oC -269
oC