Date post: | 19-Jan-2017 |
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THERMODYNAMIC RELATIONS
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Total DeferentialIf we have a function f=f(x) The derivative of a function f(x) with respect to x represents the rate of change of f with x.
Partial DifferentialsThe variation of z(x, y) with x when y is held constant is called the partial derivative of z with respect to x, and it is expressed as
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The Clapeyron Equation
Consider a Carnot heat engine operating across a small temperature difference . The corresponding saturation pressures are as shown the figures (a) and (b).
TTandT PPandP
fgLfgH sTTqandTsqThen )(
Note that, ΔT is infinitesimal and soΔ P is infinitesimal also.
Hq
Lq
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The net work is:
The four processes is steady state, hence, the work is expressed as:
And so,
Then:
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And so,
Then:
ThsThen fgfg /As:
Sustituting in dPsat/dT:This equation is called Clapeyron equation
The importance of this equation is that, we can experimentaly know dPsat/dT Also. We can measure both vf and vg
Then, we can calculate hfg and sfg
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Then:
So:
Sustituting in dPsat/dT:
For vapor-solid phase, we can use the same equation:
For very low temperature and pressure
phasesolidvaprinvvOR
phaseliquidvaprinvv
fg
fg
The vapor can be considered as ideal gas, Then: PRTv /
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Example:
Solution:
Clapeyron equation:
Arranging the equation and integrating:
Let state (1) is T=-60 C=213.2 K State (2) is T=-40 C=233.3 K
From ice-vapor table P2=0.0129 kPa and hig=2838.9 kJ/kg.
We can note that, at this range of temperature hig can be assumed constant.
Solving the integration:
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Then:
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Mathematical Relations for Homogenous PhaseFor a function f = z(x,y). The total differential of z is written as:
Where:
Taking the partial derivative of M with respect to y and of N with respect to x yields
Then:
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The equations that relate the partial derivatives of properties P, v, T, and s of a simple compressible substance to each other are called the Maxwell relations. They are obtained from the four Gibbs equations.
du T ds Pdvdh T ds v dP
The Maxwell relations
The second two Gibbs equations result from the definitions of the Helmholtz function a
And the Gibbs function g defined as
The first two of the Gibbs equations are those resulting from the internal energy u and the enthalpy h.
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Setting the second mixed partial derivatives equal for these four functions yields the Maxwell relations
Another useful relations can be derived:
v
s
T
P
a
u
h
g
These relations can be summarized by the following
figure
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Now we develop two more important relations for partial derivatives—the reciprocity and the cyclic relations. Consider the function z = z(x,y) expressed as x = x(y,z). The total differential of x is
Now combine the expressions for dx and dz.
Rearranging,
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Since y and z are independent of each other, the terms in each bracket must be zero. Thus, we obtain the reciprocity relation that shows that the inverse of a partial derivative is equal to its reciprocal.
or
The second relation is called the cyclic relation.
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Example:
Solution:
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v
s
T
P
a
u
h
g
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The constant pressure lines intersection point can be illustrated in the following figure.
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Example:
Solution:
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v
s
T
P
a
u
h
g
Substituting in 3, yields:
v
s
T
P
a
u
h
g
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Example:
Solution:
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v
s
T
P
a
u
h
g
v
s
T
P
a
u
h
g
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Example:
Solution:
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v
s
T
P
a
u
h
g
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Example:
Solution:
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Example:
Solution:
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Example:
Solution:
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v
s
T
P
a
u
h
g
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v
s
T
P
a
u
h
g
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Example:
Solution:
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v
s
T
P
a
u
h
g
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Volume Expansibility, Isothermal Compressibility and Adiabatic Compressibility
Coefficient of linear expansion: The change in length as the temperature changes, while pressure remains constant
Coefficient of volume expansion: The changes in volume as the temperature changes, while pressure remains constant
The isothermal compressibility: The change in volume as the pressure changes, while temperature remains constant
The isothermal bulk modulus: It is the reciprocal of the isothermal compressibility.
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The adiabatic compressibility: The change in volume as the pressure changes, while entropy remains constant
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Example:
Solution:
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v
s
T
P
a
u
h
g
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