chapter 5 - single phase systems notes
DESCRIPTION
mineral processing single phase systemsTRANSCRIPT
Chapter 5
Chapter 5
Single-Phase Systems
Physical PropertiesSources:1) literature (handbook, library or web sources)
2) estimation techniques (correlations or theory)
3) measurement (most expensive but sometimes required)
Liquid and Solid DensitiesTemperature dependence -- modest but sometimes important
Pressure dependence -- usually negligible (incompressible)
Mixtures -- sometimes additive volumes can be assumed
(Can you derive the last two from the first?)
Mixtures -- Nonadditive volumes
Excess Volume (per mole)
large:1) near mixture critical conditions (high T and P)
2) for strongly interacting species (e.g., ethanol + water)
Ideal Gases (sometimes called "perfect gases")
Obey the ideal gas law:
Equation of state -- a relationship between P,
, and T -- the equation above is called the ideal gas equation of state.
Compressibility factor:
definition of z
for ideal gases
Standard conditions:1) scientific0 oC, 1 atm (exact - not 1 sig. fig.)
(to 3 sig. figs.)
1 mol (at std. conditions) ( 22,400 cm3
1 lbmol ( 359 ft3
2) natural gas industry
60 oF, 14.7 psia
1 lbmol ( 379 ft3Calculations:usually involve converting from one set of conditions to another
or
Ideal gas mixtures
Partial pressure of component A:
Note: This is used as the definition of "partial pressure", even for
non-ideal gases. It is equal to the pressure that would be
exerted if A alone occupied the container only for ideal
gases.
Total pressure = sum of partial pressures:
Real Gases (sometimes called imperfect gases)
Equation of state is usually complicated -- compressibility factor not unity.
Virial equation of state -- expansion about ideal gas law:
B, C, ... = 2nd, 3rd, etc., virial coefficients (functions of T)
Cubic equations of state -- all modifications of Van der Waals equation of state:
Van der Waals equation of state
cubic in molar volume
Note: As the molar volume becomes large, z ( 1.
Soave-Redlich-Kwong equation of state
(see Eqn. 5.3-12, p. 203)
Corresponding states approach for compressibility factors
Simple (two-parameter) corresponding states: All fluids obey the
same equation of state written in reduced form.
Since zC is nearly a constant for many organic species (about 0.27), the most often used form is
see charts on pp. 208-11
They also use the following, which is helpful when the
molar volume is known:
Extended (three-parameter) corresponding states
Note: The Pitzer acentric factor is zero for simple species.
Gas mixtures
Use pseudocritical properties -- Kay's rules
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