DATOSP = 221.4 T = 395.45

bar K

V = 0.2m3/kmol

constantes Van Der Waals constantes Redlich - Kwong

3.6518 0.0428

m = M = 44kg Kg/Kmol

GASES IDEALES

P = 221.4bar

V = 0.148499155

0.2 m = 59.2595963

Van Der Walls

P = 221.4

Vtanq. =

m3

a V.W. b V.W. a R-Kw

m3/Kmol

m3

P = 221.4bar

V = 0.096106344m3/kmol

f(V) 221.4 - 42.353633 +

664.2 - 84.707266 V +

RESOLVIENDO POR EL MÉTODO NEWTON-RAPHSON0.148499155374887 0.1175488069121590.117548806912159 0.1010646218658660.101064621865866 0.0964167627759515

0.0964167627759515 0.0961075997580280.096107599758028 0.0961063442594953

0.0961063442594953 0.09610634423892110.0961063442389211 0.09610634423892110.0961063442389211 0.09610634423892110.0961063442389211 0.09610634423892110.0961063442389211 0.09610634423892110.0961063442389211 0.09610634423892110.0961063442389211 0.09610634423892110.0961063442389211 0.09610634423892110.0961063442389211 0.09610634423892110.0961063442389211 0.0961063442389211

REDLICH - KWONG

P = 221.4 m = 89.5495047

V3 V2

f I(V) V2

P = 221.4bar

m = 89.5495047

V = 0.098269667m3/Kmol

f(V) = 4402.743722 - 653.803724 -13208.23117 - 1307.60745 V -

RESOLVIENDO POR EL MÉTODO NEWTON-RAPHSON0.148499155374887 0.1180860272015560.118086027201556 0.1027970467757140.102797046775714 0.0985718755093454

0.0985718755093454 0.09827111908920520.0982711190892052 0.09826966698551780.0982696669855178 0.09826966695180490.0982696669518049 0.09826966695180490.0982696669518049 0.09826966695180490.0982696669518049 0.09826966695180490.0982696669518049 0.09826966695180490.0982696669518049 0.09826966695180490.0982696669518049 0.09826966695180490.0982696669518049 0.09826966695180490.0982696669518049 0.09826966695180490.0982696669518049 0.09826966695180490.0982696669518049 0.0982696669518049

T = 395.45K

T(V) = - 0.00220009 + 0.6960182

- 0.00330013 + 0.3480091

V3 V2

f I(V) = V2

T1.5 T0.5

T I(V) = T0.5 T -0.5

RESOLVIENDO POR EL MÉTODO NEWTON-RAPHSON395.45 482.865825620215

482.865825620215 476.116702574492476.116702574492 476.079414829895476.079414829895 476.079413684342476.079413684342 476.079413684342476.079413684342 476.079413684341476.079413684341 476.079413684342476.079413684342 476.079413684341476.079413684341 476.079413684341476.079413684341 476.079413684342476.079413684342 476.079413684342476.079413684342 476.079413684341476.079413684341 476.079413684342476.079413684342 476.079413684342476.079413684342 476.079413684342476.079413684342 476.079413684341

CARTA GENERALIZADA DEL FACTOR DE COMPRESIBILIDAD

PROPIEDADES REDUCIDAS DE GRÁFICAS:

Pr = #DIV/0!Z =

Vpr = #DIV/0!Tr = #DIV/0!

P = 0 V = 0bar

CORRELACIÓN GENERALIZADA DE PITZER

Arriba de la curva (segunda correlación)

Z = 1 +

=

#DIV/0!

#DIV/0! Z = #DIV/0!

= #DIV/0!

V = #DIV/0!m3/Kmol

m = #DIV/0!P = #DIV/0! Kg

bar

T = #DIV/0!K

B0 + wB1

B0 =

B1 =

DATOSPc =

w =Tc =

constantes Redlich - Kwong

64.5394 0.0297

R = 0.08314J/Kmol K∙

GASES IDEALES

T = 395.45K

R = 0.08314J/Kmol K∙

Kg

Van Der Walls

T = 395.45

b R-Kw

T = 395.45K

m = 91.565235kg

3.6518 V - 0.15629704

3.6518

RESOLVIENDO POR EL MÉTODO NEWTON-RAPHSON0.1175488069121590.101064621865866

0.09641676277595150.096107599758028

0.09610634425949530.09610634423892110.09610634423892110.09610634423892110.09610634423892110.09610634423892110.09610634423892110.09610634423892110.09610634423892110.09610634423892110.0961063442389211

REDLICH - KWONG

Kg

-41.2378132 V - 1.91682018

-41.2378132

RESOLVIENDO POR EL MÉTODO NEWTON-RAPHSON0.1180860272015560.102797046775714

0.09857187550934540.09827111908920520.09826966698551780.09826966695180490.09826966695180490.09826966695180490.09826966695180490.09826966695180490.09826966695180490.09826966695180490.09826966695180490.09826966695180490.09826966695180490.0982696669518049

+ 7.66722621

RESOLVIENDO POR EL MÉTODO NEWTON-RAPHSON482.865825620215476.116702574492476.079414829895476.079413684342476.079413684342476.079413684341476.079413684342476.079413684341476.079413684341476.079413684342476.079413684342476.079413684341476.079413684342476.079413684342476.079413684342476.079413684341

CARTA GENERALIZADA DEL FACTOR DE COMPRESIBILIDAD

DE GRÁFICAS:

m = #DIV/0!Kg

T = #DIV/0!m3/Kmol K

CORRELACIÓN GENERALIZADA DE PITZER

Debajo de la curva (primera correlación)

Z =

De Gráficas:

Z = 0

V = 0m3/Kmol

P = 0bar

T = #DIV/0!K

m = #DIV/0!Kg

z0 + wz1

Z0 =

Z1 =

PROPIEDADES RESIDUALES

DATOS:

P = T =bar K

Pc = Tc =

Debajo de la curva (primera correlación)

Z =

(De graficas)

Z = 0

(De graficas)

#DIV/0!m3/Kmol

(De graficas)

z0 + wz1

Z0 =

Z1 =

(De graficas)

0

0KJ/Kmol

(De graficas)

(De graficas)

0

0KJ/Kmol

HR =

SR =

PROPIEDADES RESIDUALES

Pr =

Localizar valores en la graficaw =

Tr = #DIV/0!

Arriba de la curva ( segunda correlación)

#DIV/0!

#DIV/0!

#DIV/0!

z = #DIV/0!

#DIV/0!m3/Kmol

#DIV/0!

#DIV/0!

#DIV/0!

#DIV/0!KJ/Kmol

#DIV/0!

#DIV/0!KJ/Kmol