chapter 5 - single phase systems notes

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Chapter 5 Single-Phase Systems Physical Properties Sources: 1) literature (handbook, library or web sources) 2) estimation techniques (correlations or theory) 3) measurement (most expensive but sometimes required) Liquid and Solid Densities emperature dependence !! modest but sometimes important "ressure dependence !! usually ne#li#ible ( incompressible ) $ixtures !! sometimes additive volumes can be assumed V V i = 1 ρ ρ = w i i ρ = = M V x M x V i i i i (%an you derive the last two &rom the &irst') $ixtures !! Nonadditive volumes V x V V i i E = + xcess olume (per mole) V E lar#e: 1) near mixture critical conditions (hi#h and ") 2) &or stron#ly interactin# species (e*#*, ethanol + wate Ideal Gases (sometimes called per&ect #ases ) -bey the ideal #as law: PV nRT PV RT = = quation o& state !! a relationship between P, V , and T !! the equation above is called the ideal #as equation o& state*

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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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