THERMODYNAMICS - THEORY
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Entropy Change of Pure Substances
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The Entropy of a Pure Substance Determined by Tables
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The entropy of a pure substance is determined from
tables in the same manner as other properties such as v, u, and h. The value of entropy at a specified state is determined just like any other property.
- Compressed liquid: from tables
- Saturated liquid (sf): from tables
- Saturated mixture: s = sf + xsfg
where
x = quality
sfg = sg - sf
- Saturated vapor (sg): from tables
- Superheated vapor: from tables
If the compressed liquid data are not available, the entropy of the
compressed liquid can be approximated by the saturated liquid at the same temperature.
scompressed@T,P = sf@T |
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Water Tables |
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Entropy
Change of Solids and Liquids
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For an incompressible substances, the specific volume does not change
during a process. That is,
dv = 0
The
internal energy of an incompressible substance is
du = c(T) dT
Most solids and liquids can be approximated
as incompressible substances. The entropy change of solids and liquids
can be obtained by applying the above two equations to the
first Tds equation.
The entropy change during a process 1-2 is
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Constant Specific Heat Used in Small Temperature
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If the temperature variation (T2 - T1) is
small over the entire process, an average specific heat (cave)
is used and treated as a constant (constant-specific-heats assumption).
Then
the entropy change can be evaluated by
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Entropy Change of Ideal Gases
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The property relations for
ideal gases are:
pv = RT
du = cvdT
dh = cPdT
The first relation of entropy change for ideal gases is obtained
by replacing P by RT/v and du by cvdT in the
first Tds equation:
Tds = du + Pdv
= cvdT + RTdv/v
ds = cvdT/T + Rdv/v
Integrating ds from state 1 to state 2 gives the first relation of
entropy change for ideal gases.
The second relation of entropy change for ideal gases is obtained
by replacing v by RT/P and dh by cPdT in the
second Tds equation:
Tds = dh - vdP
= cPdT - RTdP/P
ds = cPdT/T - RdP/P
Integrating ds from state 1 to state 2 gives the second relation of
entropy change for ideal gases.
A common approximation is made by assuming that the specific
heats of ideal gases are constants if the temperature variation is
small (constant-specific-heats assumption). Replacing cv and
cP with constants cv,av and cP,av in
the first and second relations of entropy change and integrating from state
1 to state 2 gives,
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Function s0 is a Function of
Temperature only
Ideal-gas Properties of Air Table
Approximate Analysis and
Exact Analysis of Entropy Change
during a Cooling Process
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If the temperature variation is large, the variation of specific
heats with temperature should be considered and relations between
cv(T), cP(T) and temperature are needed to integrate
the first and second relations. For convenience, a
function s0, standard-state entropy, is defined as
s0 is a function of temperature only and is tabulated
with temperature. Absolute zero is used
as the reference temperature.
Replacing T as T1 and T2 in the above definition gives
Then the entropy change of ideal gases during a process 1-2 is
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