Universidad nacional del callao FIQ-UNAC

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO

DE LECHO FIJO CON DIFUSIÓN RADIAL

El componente a disuelto en un fluido esta fluyendo en un reactor catalítico, cuya

cinética es de primer orden, irreversible los datos del reactor y operación del mismo se

muestran a continuación:

R: radio del reactor =0.0625pies

L: longitud del reactor =0.20 pies

Vz: velocidad media del fluido =2500pies/h

ΔH: entalpia de reacción = -30000 btu/h

ρ: densidad media de la mezcla reaccionantes =0.1lb/pie3

CA0=concentración inicial de A =0.002 lb/pie3

RA= -ra.Cao .ρc : velocidad de reacción de A, dada en lb/h.pie3

rA=19600(1-x)exp(-97007T)en ft3/h lb de catalizador

T: temperatura de sistema, ºR

Δr: variación radial =0.0125pies

Δz: variación longitudinal =0.05pies

X: conversión de A ,lb de A reaccionado/lb de A en la alimentación

Cp: calor especifico de la mezcla =0.2btu/lbºF

G=ΔHr.Ra

Perfil de temperatura, esta dada por:

Distribución

desde el centro

del tubo(pies)

temperatura (ºF)

0.000 600

0.0125 600

0.0250 600

0.0375 600

0.050 600

0.0625 555

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN

RADIAL

Universidad nacional del callao FIQ-UNAC

Caso I: sin la difusión radial ni axial

1. Balance de matéria (coordenadas cilíndricas)

Considerando:

Flujo estacionário

Velocidad constante

Flujo axial

Sin Difusion

Se tiene La siguiente ecuación:

Se sabe:

............................(3)

Reemplazando (3) em (2) y Ra

RA= - ra.Cao .ρc

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN

RADIAL

Universidad nacional del callao FIQ-UNAC

Simplificando Cao

Reemplazando datos:

rA=19600(1-x)exp(-97007T)

2. Balance de energia (coordenadas cilíndricas)

Considerando:

Flujo estacionário

Velocidad constante

Flujo axial

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN

RADIAL

Universidad nacional del callao FIQ-UNAC

Sin Difusion

Se tiene La siguiente ecuación

Si:

G=ΔHr.Ra

Dividir entra VZ y reemplazar

RA= -ra.Cao .ρc

rA=19600(1-x)exp(-97007T)

Reemplazar datos:

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN

RADIAL

Universidad nacional del callao FIQ-UNAC

POLYMATH Report

Ordinary Differential Equations 29-Sep-2009

Calculated values of DEQ variables

  Variable Initial value Minimal value Maximal value Final value

1 Z 0 0 4. 4.

2 X 0 0 1. 1.

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN

RADIAL

Universidad nacional del callao FIQ-UNAC

3 T 1060. 1060. 4060. 4060.

4 dc 100. 100. 100. 100.

5 V 2500. 2500. 2500. 2500.

6 DELH -3.0E+04 -3.0E+04 -3.0E+04 -3.0E+04

7 d 0.1 0.1 0.1 0.1

8 Co 0.002 0.002 0.002 0.002

9 Cp 0.2 0.2 0.2 0.2

10 e 2.718282 2.718282 2.718282 2.718282

Differential equations

1 d(X)/d(Z) = (dc / V) * 19600 * (1 - X) * (e ^ (-9700 / T))

2 d(T)/d(Z) = -((DELH * Co * dc) / (V * d * Cp)) * 19600 * (1 - X) * (e ^ (-9700 / T))

Explicit equations

1 dc = 100

2 V = 2500

3 DELH = -30000

4 d = 0.1

5 Co = 0.002

6 Cp = 0.2

7 e = 2.718281828

General

Total number of equations 9

Number of differential equations 2

Number of explicit equations 7

Elapsed time 0.000 sec

Solution method RKF_45

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN

RADIAL

Universidad nacional del callao FIQ-UNAC

Step size guess. h 0.000001

Truncation error tolerance. eps 0.000001

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN

RADIAL

Universidad nacional del callao FIQ-UNAC

z X T dc V DELH d Co Cp e

0 0 1060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.1091002 0.0102613 1090.784 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.1411002 0.013816 1101.448 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.1731002 0.0176867 1113.06 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.2051002 0.0219264 1125.779 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.2691002 0.0317944 1155.383 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.3011002 0.0376159 1172.848 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.3331002 0.04421 1192.63 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.3651002 0.0517725 1215.318 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.4291002 0.0710207 1273.062 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.4591372 0.0828431 1308.529 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.4859397 0.0956733 1347.02 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.5305418 0.1244335 1433.3 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.5651558 0.1578176 1533.453 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.6032449 0.218316 1714.948 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.6439683 0.3569032 2130.71 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.6837613 0.6986445 3155.933 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.7221541 0.9634501 3950.35 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.7610239 0.9976219 4052.866 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.8021094 0.9998755 4059.627 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.8479274 0.9999954 4059.986 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.88413 0.9999997 4059.999 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.9409348 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

0.9729348 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.004935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.068935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.100935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.132935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.164935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.228935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.260935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.292935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.324935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN

RADIAL

Universidad nacional del callao FIQ-UNAC

1.388935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.420935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.452935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.484935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.548935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.580935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.612935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.644935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.708935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.740935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.772935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.804935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.868935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.900935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.932935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

1.964935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.028935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.060935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.092935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.124935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.188935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.220935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.252935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.284935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.348935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.380935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.412935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.444935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.508935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.540935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.572935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.604935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.668935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.700935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN

RADIAL

Universidad nacional del callao FIQ-UNAC

2.732935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.764935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.828935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.860935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.892935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.924935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

2.988935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.020935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.052935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.084935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.148935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.180935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.212935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.244935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.308935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.340935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.372935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.404935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.468935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.500935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.532935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.564935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.628935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.660935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.692935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.724935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.788935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.820935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.852935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.884935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.948935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

3.980935 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

4 1 4060 100 2500 -3.00E+04 0.1 0.002 0.2 2.718282

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN

RADIAL

Universidad nacional del callao FIQ-UNAC

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

Cálculo de la longitud del reactor

*De la gráfica se obtuvo la longitud del reactor L:

Cálculo del volumen del reactor tubular

Cálculo del volumen del catalizador

Por lo tanto la masa de l catalizador es:

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON

DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

Caso II: Considerando difusión axial y radial

*Ecuación de Balance de Energía

…(1)

*Ecuación de Balance de Masa

…(2)

Además

Para el balance de Energía

De la ecuación (1)

…(*)

Sea:

Reemplazando φ1 y φ2 en (*)

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON

DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

…(3)

Para el balance de Masa

De la ecuación (2)

…(**)

Pero se sabe que:

Reemplazando en la ecuación (**)

…(***)

Sea:

Reemplazando φ3 y φ4 en (***)

…(4)

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON

DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

*Para resolver las ecuaciones (3) y (4) necesitamos convertirlas a ecuaciones

diferenciales ordinarias (EDO), por lo tanto se discretizará las derivadas con

respecto a ‘r’, y se resolverá el sistema de ecuaciones diferenciales ordinarias

(SEDO), para cada punto de la partición de r; obteniendo los valores de T y X

en función de Z.

Discretizando la ecuación (3)

Factorizando y ordenando

; … (5)

Discretizando la ecuación (4)

Factorizando y ordenando

; … (6)

Analizando para r = 0

Para r = 0 las ecuaciones (3) y (4) son indeterminadas, debido a esto aplicamos el teorema de L’Hospital para eliminar la indeterminación en ambos casos.

…($)

…($$)

Reemplazando ($) y ($$) en (3) y (4) respectivamente

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON

DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

…(7)

…(8)

Discretizando la ecuación (7)

Factorizando y ordenando

… (9)

Discretizando la ecuación (8)

Factorizando y ordenando

… (10)

*Cuando r = 0, la posición es el centro del tubo y se cumple que:

…(&)

…(&&)

Reemplazando (&) y (&&) en (9) y (10) respectivamente

En (9)

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON

DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

; … (11)

En (10)

; … (12)

Reemplazando valores de i:

Para i = 0; reemplazando en las ecuaciones (11) y (12)

…(13)

…(14)

Para V i > 0; reemplazando en las ecuaciones (5) y (6)

Para i = 1

… (15)

… (16)

Para i = 2

… (17)

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON

DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

… (18)

Para i = 3

… (19)

… (20)

Para i = 4

… (21)

… (22)

Para i = 5

… (23)

… (24)

Para i = 6

… (25)

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON

DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

… (26)

Para i = 7

… (27)

… (28)

Para i = 8

… (29)

… (30)

Para i = 9

… (31)

… (32)

Para i = 10

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON

DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

… ( @ )

Pero sabemos que:

…( @ @ )

Reemplazando ( @ @ ) en ( @ )

… (33)

Cálculo de las constantes

*

*

*

*

*

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON

DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON

DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

Resolviendo el sistema de ecuaciones diferenciales ordinarias desde la ecuación (13) hasta la ecuación (33) con el software Polymath 6.0, se obtuvieron los siguientes resultados:

*Valores para T en función de Z y de r :

r0=0 r1=0.00625 r2=0.0125 r3=0.01875 r4=0.025 r5=0.03125 r6=0.0375 r7=0.04375 r8=0.05 r9=0.05625 r10=0.0625Z T0 T1 T2 T3 T4 T5 T6 T7 T8 T9 T100 1060 1060 1060 1060 1060 1060 1060 1060 1060 1060 1015

0.0241633 1066.187 1066.187 1066.187 1066.187 1066.187 1066.187 1066.187 1066.187 1066.187 1066.184 10150.0321633 1068.306 1068.306 1068.306 1068.306 1068.306 1068.306 1068.306 1068.306 1068.306 1068.302 10150.0401633 1070.463 1070.463 1070.463 1070.463 1070.463 1070.463 1070.463 1070.463 1070.463 1070.458 10150.0561633 1074.894 1074.894 1074.894 1074.894 1074.894 1074.894 1074.894 1074.894 1074.894 1074.886 10150.0641633 1077.17 1077.17 1077.17 1077.17 1077.17 1077.17 1077.17 1077.17 1077.17 1077.161 10150.0721633 1079.488 1079.488 1079.488 1079.488 1079.488 1079.488 1079.488 1079.488 1079.488 1079.478 10150.0801633 1081.85 1081.85 1081.85 1081.85 1081.85 1081.85 1081.85 1081.85 1081.85 1081.839 10150.0961633 1086.712 1086.712 1086.712 1086.712 1086.712 1086.712 1086.712 1086.712 1086.712 1086.698 10150.1041633 1089.215 1089.215 1089.215 1089.215 1089.215 1089.215 1089.215 1089.215 1089.215 1089.199 10150.1121633 1091.767 1091.767 1091.767 1091.767 1091.767 1091.767 1091.767 1091.767 1091.767 1091.75 10150.1201633 1094.372 1094.372 1094.372 1094.372 1094.372 1094.372 1094.372 1094.372 1094.372 1094.353 10150.1361633 1099.744 1099.744 1099.744 1099.744 1099.744 1099.744 1099.744 1099.744 1099.744 1099.721 10150.1441633 1102.516 1102.516 1102.516 1102.516 1102.516 1102.516 1102.516 1102.516 1102.516 1102.491 10150.1521633 1105.348 1105.348 1105.348 1105.348 1105.348 1105.348 1105.348 1105.348 1105.348 1105.321 10150.1601633 1108.242 1108.242 1108.242 1108.242 1108.242 1108.242 1108.242 1108.242 1108.242 1108.213 10150.1761633 1114.227 1114.227 1114.227 1114.227 1114.227 1114.227 1114.227 1114.227 1114.227 1114.193 10150.1841633 1117.323 1117.323 1117.323 1117.323 1117.323 1117.323 1117.323 1117.323 1117.323 1117.287 10150.1921633 1120.492 1120.492 1120.492 1120.492 1120.492 1120.492 1120.492 1120.492 1120.492 1120.453 10150.2001633 1123.737 1123.737 1123.737 1123.737 1123.737 1123.737 1123.737 1123.737 1123.737 1123.696 10150.2161633 1130.468 1130.468 1130.468 1130.468 1130.468 1130.468 1130.468 1130.468 1130.468 1130.421 10150.2241633 1133.961 1133.961 1133.961 1133.961 1133.961 1133.961 1133.961 1133.961 1133.961 1133.911 1015

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

0.2321633 1137.545 1137.545 1137.545 1137.545 1137.545 1137.545 1137.545 1137.545 1137.545 1137.491 10150.2401633 1141.222 1141.222 1141.222 1141.222 1141.222 1141.222 1141.222 1141.222 1141.222 1141.165 10150.2561633 1148.878 1148.878 1148.878 1148.878 1148.878 1148.878 1148.878 1148.878 1148.878 1148.814 10150.2641633 1152.866 1152.866 1152.866 1152.866 1152.866 1152.866 1152.866 1152.866 1152.866 1152.798 10150.2721633 1156.967 1156.967 1156.967 1156.967 1156.967 1156.967 1156.967 1156.967 1156.967 1156.896 10150.2801633 1161.189 1161.189 1161.189 1161.189 1161.189 1161.189 1161.189 1161.189 1161.189 1161.113 10150.2961633 1170.015 1170.015 1170.015 1170.015 1170.015 1170.015 1170.015 1170.015 1170.015 1169.93 10150.3041633 1174.633 1174.633 1174.633 1174.633 1174.633 1174.633 1174.633 1174.633 1174.633 1174.544 10150.3121633 1179.399 1179.399 1179.399 1179.399 1179.399 1179.399 1179.399 1179.399 1179.399 1179.305 10150.3201633 1184.32 1184.32 1184.32 1184.32 1184.32 1184.32 1184.32 1184.32 1184.32 1184.221 10150.3361633 1194.665 1194.665 1194.665 1194.665 1194.665 1194.665 1194.665 1194.665 1194.665 1194.556 10150.3441633 1200.109 1200.109 1200.109 1200.109 1200.109 1200.109 1200.109 1200.109 1200.109 1199.995 10150.3521633 1205.749 1205.749 1205.749 1205.749 1205.749 1205.749 1205.749 1205.749 1205.75 1205.629 10150.3601633 1211.598 1211.598 1211.598 1211.598 1211.598 1211.598 1211.598 1211.598 1211.598 1211.472 10150.3761633 1223.977 1223.977 1223.977 1223.977 1223.977 1223.977 1223.977 1223.977 1223.977 1223.838 10150.3841633 1230.539 1230.539 1230.539 1230.539 1230.539 1230.539 1230.539 1230.539 1230.539 1230.393 10150.3921633 1237.371 1237.371 1237.371 1237.371 1237.371 1237.371 1237.371 1237.371 1237.372 1237.219 10150.4001633 1244.495 1244.495 1244.495 1244.495 1244.495 1244.495 1244.495 1244.495 1244.496 1244.336 10150.4161633 1259.707 1259.707 1259.707 1259.707 1259.707 1259.707 1259.707 1259.707 1259.707 1259.532 10150.4241633 1267.845 1267.845 1267.845 1267.845 1267.845 1267.845 1267.845 1267.845 1267.846 1267.662 10150.4321633 1276.378 1276.378 1276.378 1276.378 1276.378 1276.378 1276.378 1276.378 1276.378 1276.187 10150.4401633 1285.338 1285.338 1285.338 1285.338 1285.338 1285.338 1285.338 1285.338 1285.339 1285.139 10150.4561633 1304.697 1304.697 1304.697 1304.697 1304.697 1304.697 1304.697 1304.698 1304.699 1304.481 10150.4641633 1315.187 1315.187 1315.187 1315.187 1315.187 1315.187 1315.187 1315.187 1315.189 1314.961 10150.4721633 1326.288 1326.288 1326.288 1326.288 1326.288 1326.288 1326.288 1326.288 1326.289 1326.053 10150.4801633 1338.061 1338.061 1338.061 1338.061 1338.061 1338.061 1338.061 1338.061 1338.063 1337.817 10150.4961633 1363.923 1363.923 1363.923 1363.923 1363.923 1363.923 1363.923 1363.923 1363.925 1363.66 10150.5041633 1378.189 1378.189 1378.189 1378.189 1378.189 1378.189 1378.189 1378.189 1378.192 1377.918 10150.5121633 1393.488 1393.488 1393.488 1393.488 1393.488 1393.488 1393.488 1393.488 1393.492 1393.209 10150.5201633 1409.952 1409.952 1409.952 1409.952 1409.952 1409.952 1409.952 1409.952 1409.956 1409.666 10150.5361633 1447.016 1447.016 1447.016 1447.016 1447.016 1447.016 1447.016 1447.016 1447.022 1446.72 10150.5441633 1468.021 1468.021 1468.021 1468.021 1468.021 1468.021 1468.021 1468.021 1468.027 1467.723 1015

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

0.5521633 1491.012 1491.012 1491.012 1491.012 1491.012 1491.012 1491.012 1491.013 1491.02 1490.717 10150.5601633 1516.316 1516.316 1516.316 1516.316 1516.316 1516.316 1516.316 1516.316 1516.325 1516.028 10150.5761633 1575.559 1575.559 1575.559 1575.559 1575.559 1575.559 1575.559 1575.559 1575.571 1575.309 10150.5841633 1610.622 1610.622 1610.622 1610.622 1610.622 1610.622 1610.622 1610.623 1610.638 1610.412 10150.5921633 1650.323 1650.323 1650.323 1650.323 1650.323 1650.323 1650.323 1650.323 1650.342 1650.172 10150.6001633 1695.689 1695.689 1695.689 1695.689 1695.689 1695.689 1695.689 1695.689 1695.713 1695.629 10150.6161633 1809.217 1809.217 1809.217 1809.217 1809.217 1809.217 1809.217 1809.217 1809.254 1809.495 10150.6241633 1881.496 1881.496 1881.496 1881.496 1881.496 1881.496 1881.496 1881.497 1881.544 1882.079 10150.631876 1964.628 1964.628 1964.628 1964.628 1964.628 1964.628 1964.628 1964.628 1964.69 1965.652 10150.6453867 2153.744 2153.744 2153.744 2153.744 2153.744 2153.744 2153.744 2153.745 2153.845 2156.146 10150.6513759 2260.928 2260.928 2260.928 2260.928 2260.928 2260.928 2260.928 2260.929 2261.053 2264.335 10150.6623723 2505.957 2505.957 2505.957 2505.957 2505.957 2505.957 2505.957 2505.959 2506.143 2512.204 10150.6728704 2803.193 2803.193 2803.193 2803.193 2803.193 2803.193 2803.193 2803.196 2803.452 2813.614 10150.6850063 3196.623 3196.623 3196.623 3196.623 3196.623 3196.623 3196.623 3196.626 3196.947 3212.862 10150.6920407 3416.586 3416.586 3416.586 3416.586 3416.586 3416.586 3416.586 3416.59 3416.919 3435.701 10150.7035034 3704.703 3704.703 3704.703 3704.703 3704.703 3704.703 3704.703 3704.705 3704.999 3726.673 10150.7113028 3837.57 3837.57 3837.57 3837.57 3837.57 3837.57 3837.57 3837.572 3837.826 3860.539 10150.7221758 3950.51 3950.51 3950.51 3950.51 3950.51 3950.51 3950.51 3950.511 3950.716 3974.642 10150.7334958 4009.683 4009.683 4009.683 4009.683 4009.683 4009.683 4009.683 4009.684 4009.856 4035.452 10150.7417022 4031.736 4031.736 4031.736 4031.736 4031.736 4031.736 4031.736 4031.737 4031.896 4059.051 10150.7507019 4045.084 4045.084 4045.084 4045.084 4045.084 4045.084 4045.084 4045.084 4045.236 4074.376 10150.7607625 4052.731 4052.731 4052.731 4052.731 4052.731 4052.731 4052.731 4052.731 4052.88 4084.479 10150.7722304 4056.805 4056.805 4056.805 4056.805 4056.805 4056.805 4056.805 4056.806 4056.955 4091.55 10150.785592 4058.776 4058.776 4058.776 4058.776 4058.776 4058.776 4058.776 4058.777 4058.93 4097.157 10150.7931977 4059.291 4059.291 4059.291 4059.291 4059.291 4059.291 4059.291 4059.292 4059.448 4099.779 10150.8011977 4059.601 4059.601 4059.601 4059.601 4059.601 4059.601 4059.601 4059.602 4059.762 4102.32 10150.8171977 4059.874 4059.874 4059.874 4059.874 4059.874 4059.874 4059.874 4059.874 4060.042 4107.078 10150.8251977 4059.929 4059.929 4059.929 4059.929 4059.929 4059.929 4059.929 4059.929 4060.101 4109.38 10150.8331977 4059.96 4059.96 4059.96 4059.96 4059.96 4059.96 4059.96 4059.96 4060.136 4111.658 10150.8411977 4059.978 4059.978 4059.978 4059.978 4059.978 4059.978 4059.978 4059.978 4060.158 4113.922 10150.8571977 4059.993 4059.993 4059.993 4059.993 4059.993 4059.993 4059.993 4059.993 4060.181 4118.424 10150.8651977 4059.996 4059.996 4059.996 4059.996 4059.996 4059.996 4059.996 4059.996 4060.189 4120.667 1015

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

0.8731977 4059.998 4059.998 4059.998 4059.998 4059.998 4059.998 4059.998 4059.998 4060.195 4122.906 10150.8811977 4059.999 4059.999 4059.999 4059.999 4059.999 4059.999 4059.999 4059.999 4060.2 4125.142 10150.8971977 4060 4060 4060 4060 4060 4060 4060 4060 4060.21 4129.604 10150.9051977 4060 4060 4060 4060 4060 4060 4060 4060 4060.214 4131.831 10150.9131977 4060 4060 4060 4060 4060 4060 4060 4060 4060.219 4134.055 10150.9211977 4060 4060 4060 4060 4060 4060 4060 4060 4060.223 4136.276 10150.9371977 4060 4060 4060 4060 4060 4060 4060 4060 4060.232 4140.709 10150.9451977 4060 4060 4060 4060 4060 4060 4060 4060 4060.237 4142.922 10150.9531977 4060 4060 4060 4060 4060 4060 4060 4060 4060.242 4145.132 10150.9611977 4060 4060 4060 4060 4060 4060 4060 4060 4060.246 4147.339 10150.9771977 4060 4060 4060 4060 4060 4060 4060 4060.001 4060.256 4151.745 10150.9851977 4060 4060 4060 4060 4060 4060 4060 4060.001 4060.26 4153.944 10150.9931977 4060 4060 4060 4060 4060 4060 4060 4060.001 4060.265 4156.14 1015

1 4060 4060 4060 4060 4060 4060 4060 4060.001 4060.269 4158.005 1015

*Valores para T en función de Z y de r :

r0=0 r1=0.00625 r2=0.0125 r3=0.01875 r4=0.025 r5=0.03125 r6=0.0375 r7=0.04375 r8=0.05 r9=0.05625 r10=0.0625Z X0 X1 X2 X3 X4 X5 X6 X7 X8 X9 X10

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

0 0 0 0 0 0 0 0 0 0 0 00.0241633 0.0020622 0.0020622 0.0020622 0.0020622 0.0020622 0.0020622 0.0020622 0.0020622 0.0020622 0.0020613 0.00133980.0321633 0.0027687 0.0027687 0.0027687 0.0027687 0.0027687 0.0027687 0.0027687 0.0027687 0.0027687 0.0027671 0.00178330.0401633 0.0034877 0.0034877 0.0034877 0.0034877 0.0034877 0.0034877 0.0034877 0.0034877 0.0034877 0.0034851 0.00222690.0561633 0.0049645 0.0049645 0.0049645 0.0049645 0.0049645 0.0049645 0.0049645 0.0049645 0.0049645 0.0049594 0.0031140.0641633 0.0057232 0.0057232 0.0057232 0.0057232 0.0057232 0.0057232 0.0057232 0.0057232 0.0057232 0.0057164 0.00355760.0721633 0.0064961 0.0064961 0.0064961 0.0064961 0.0064961 0.0064961 0.0064961 0.0064961 0.006496 0.0064873 0.00400130.0801633 0.0072835 0.0072835 0.0072835 0.0072835 0.0072835 0.0072835 0.0072835 0.0072835 0.0072835 0.0072725 0.0044450.0961633 0.008904 0.008904 0.008904 0.008904 0.008904 0.008904 0.008904 0.008904 0.008904 0.0088877 0.00533260.1041633 0.0097383 0.0097383 0.0097383 0.0097383 0.0097383 0.0097383 0.0097383 0.0097383 0.0097382 0.0097188 0.00577650.1121633 0.0105892 0.0105892 0.0105892 0.0105892 0.0105892 0.0105892 0.0105892 0.0105892 0.0105891 0.0105662 0.00622050.1201633 0.0114573 0.0114573 0.0114573 0.0114573 0.0114573 0.0114573 0.0114573 0.0114573 0.0114572 0.0114306 0.00666460.1361633 0.0132481 0.0132481 0.0132481 0.0132481 0.0132481 0.0132481 0.0132481 0.0132481 0.013248 0.0132126 0.00755320.1441633 0.0141721 0.0141721 0.0141721 0.0141721 0.0141721 0.0141721 0.0141721 0.0141721 0.0141719 0.0141316 0.00799770.1521633 0.015116 0.015116 0.015116 0.015116 0.015116 0.015116 0.015116 0.015116 0.0151158 0.0150702 0.00844240.1601633 0.0160807 0.0160807 0.0160807 0.0160807 0.0160807 0.0160807 0.0160807 0.0160807 0.0160804 0.0160291 0.00888720.1761633 0.0180757 0.0180757 0.0180757 0.0180757 0.0180757 0.0180757 0.0180757 0.0180757 0.0180753 0.0180112 0.00977750.1841633 0.0191077 0.0191077 0.0191077 0.0191077 0.0191077 0.0191077 0.0191077 0.0191077 0.0191073 0.0190361 0.0102230.1921633 0.0201641 0.0201641 0.0201641 0.0201641 0.0201641 0.0201641 0.0201641 0.0201641 0.0201636 0.0200848 0.01066870.2001633 0.0212458 0.0212458 0.0212458 0.0212458 0.0212458 0.0212458 0.0212458 0.0212457 0.0212452 0.0211584 0.01111460.2161633 0.0234894 0.0234894 0.0234894 0.0234894 0.0234894 0.0234894 0.0234894 0.0234894 0.0234887 0.0233841 0.01200740.2241633 0.0246538 0.0246538 0.0246538 0.0246538 0.0246538 0.0246538 0.0246538 0.0246538 0.024653 0.0245386 0.01245420.2321633 0.0258482 0.0258482 0.0258482 0.0258482 0.0258482 0.0258482 0.0258482 0.0258482 0.0258473 0.0257226 0.01290140.2401633 0.027074 0.027074 0.027074 0.027074 0.027074 0.027074 0.027074 0.027074 0.027073 0.0269374 0.01334890.2561633 0.0296259 0.0296259 0.0296259 0.0296259 0.0296259 0.0296259 0.0296259 0.0296259 0.0296247 0.0294651 0.01424510.2641633 0.0309552 0.0309552 0.0309552 0.0309552 0.0309552 0.0309552 0.0309552 0.0309552 0.0309539 0.0307813 0.01469390.2721633 0.0323225 0.0323225 0.0323225 0.0323225 0.0323225 0.0323225 0.0323225 0.0323224 0.032321 0.0321347 0.0151430.2801633 0.0337295 0.0337295 0.0337295 0.0337295 0.0337295 0.0337295 0.0337295 0.0337295 0.0337279 0.0335271 0.01559270.2961633 0.0366715 0.0366715 0.0366715 0.0366715 0.0366715 0.0366715 0.0366715 0.0366715 0.0366695 0.0364374 0.01649360.3041633 0.038211 0.038211 0.038211 0.038211 0.038211 0.038211 0.038211 0.038211 0.0382089 0.0379598 0.01694490.3121633 0.0397996 0.0397996 0.0397996 0.0397996 0.0397996 0.0397996 0.0397996 0.0397996 0.0397972 0.0395303 0.01739680.3201633 0.04144 0.04144 0.04144 0.04144 0.04144 0.04144 0.04144 0.04144 0.0414374 0.0411516 0.0178493

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

0.3361633 0.0448883 0.0448883 0.0448883 0.0448883 0.0448883 0.0448883 0.0448883 0.0448883 0.0448852 0.0445589 0.01875650.3441633 0.046703 0.046703 0.046703 0.046703 0.046703 0.046703 0.046703 0.046703 0.0466997 0.0463515 0.01921120.3521633 0.0485831 0.0485831 0.0485831 0.0485831 0.0485831 0.0485831 0.0485831 0.0485831 0.0485795 0.0482083 0.01966670.3601633 0.0505327 0.0505327 0.0505327 0.0505327 0.0505327 0.0505327 0.0505327 0.0505327 0.0505288 0.0501334 0.02012310.3761633 0.0546591 0.0546591 0.0546591 0.0546591 0.0546591 0.0546591 0.0546591 0.054659 0.0546545 0.0542069 0.02103860.3841633 0.0568462 0.0568462 0.0568462 0.0568462 0.0568462 0.0568462 0.0568462 0.0568462 0.0568413 0.0563656 0.02149790.3921633 0.0591238 0.0591238 0.0591238 0.0591238 0.0591238 0.0591238 0.0591238 0.0591238 0.0591185 0.0586133 0.02195820.4001633 0.0614985 0.0614985 0.0614985 0.0614985 0.0614985 0.0614985 0.0614985 0.0614984 0.0614927 0.0609565 0.02241970.4161633 0.0665689 0.0665689 0.0665689 0.0665689 0.0665689 0.0665689 0.0665689 0.0665688 0.0665623 0.0659592 0.02334640.4241633 0.0692817 0.0692817 0.0692817 0.0692817 0.0692817 0.0692817 0.0692817 0.0692816 0.0692746 0.0686355 0.02381180.4321633 0.0721259 0.0721259 0.0721259 0.0721259 0.0721259 0.0721259 0.0721259 0.0721258 0.0721183 0.0714414 0.02427860.4401633 0.0751126 0.0751126 0.0751126 0.0751126 0.0751126 0.0751126 0.0751126 0.0751126 0.0751045 0.0743878 0.0247470.4561633 0.0815658 0.0815658 0.0815658 0.0815658 0.0815658 0.0815658 0.0815658 0.0815657 0.0815566 0.080754 0.0256890.4641633 0.0850624 0.0850624 0.0850624 0.0850624 0.0850624 0.0850624 0.0850624 0.0850623 0.0850526 0.0842037 0.02616280.4721633 0.0887625 0.0887625 0.0887625 0.0887625 0.0887625 0.0887625 0.0887625 0.0887624 0.088752 0.0878545 0.02663870.4801633 0.0926869 0.0926869 0.0926869 0.0926869 0.0926869 0.0926869 0.0926869 0.0926868 0.0926758 0.0917269 0.02711670.4961633 0.1013075 0.1013075 0.1013075 0.1013075 0.1013075 0.1013075 0.1013075 0.1013074 0.1012949 0.1002352 0.02808020.5041633 0.1060629 0.1060629 0.1060629 0.1060629 0.1060629 0.1060629 0.1060629 0.1060628 0.1060496 0.1049299 0.02856590.5121633 0.1111628 0.1111628 0.1111628 0.1111628 0.1111628 0.1111628 0.1111628 0.1111627 0.1111487 0.1099658 0.02905470.5201633 0.1166506 0.1166506 0.1166506 0.1166506 0.1166506 0.1166506 0.1166506 0.1166505 0.1166357 0.1153862 0.02954680.5361633 0.1290055 0.1290055 0.1290055 0.1290055 0.1290055 0.1290055 0.1290055 0.1290053 0.1289889 0.127595 0.0305420.5441633 0.1360069 0.1360069 0.1360069 0.1360069 0.1360069 0.1360069 0.1360069 0.1360067 0.1359895 0.1345176 0.03104580.5521633 0.1436708 0.1436708 0.1436708 0.1436708 0.1436708 0.1436708 0.1436708 0.1436706 0.1436526 0.1420986 0.03155440.5601633 0.1521054 0.1521054 0.1521054 0.1521054 0.1521054 0.1521054 0.1521054 0.1521052 0.1520864 0.150446 0.03206820.5761633 0.1718529 0.1718529 0.1718529 0.1718529 0.1718529 0.1718529 0.1718529 0.1718526 0.1718323 0.1700069 0.03311420.5841633 0.1835408 0.1835408 0.1835408 0.1835408 0.1835408 0.1835408 0.1835408 0.1835406 0.1835196 0.1815962 0.0336480.5921633 0.1967742 0.1967742 0.1967742 0.1967742 0.1967742 0.1967742 0.1967742 0.196774 0.1967527 0.1947287 0.03419010.6001633 0.2118964 0.2118964 0.2118964 0.2118964 0.2118964 0.2118964 0.2118964 0.2118961 0.2118746 0.2097492 0.0347420.6161633 0.249739 0.249739 0.249739 0.249739 0.249739 0.249739 0.249739 0.2497387 0.2497183 0.2474018 0.03588150.6241633 0.273832 0.273832 0.273832 0.273832 0.273832 0.273832 0.273832 0.2738318 0.273813 0.2714207 0.03647340.631876 0.3015425 0.3015425 0.3015425 0.3015425 0.3015425 0.3015425 0.3015425 0.3015424 0.3015263 0.2990896 0.03706170.6453867 0.3645814 0.3645814 0.3645814 0.3645814 0.3645814 0.3645814 0.3645814 0.3645814 0.3645746 0.3621984 0.0381453

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

0.6513759 0.4003092 0.4003092 0.4003092 0.4003092 0.4003092 0.4003092 0.4003092 0.4003092 0.4003091 0.3980588 0.03865310.6623723 0.4819858 0.4819858 0.4819858 0.4819858 0.4819858 0.4819858 0.4819858 0.481986 0.4820036 0.4802473 0.03964240.6728704 0.5810644 0.5810644 0.5810644 0.5810644 0.5810644 0.5810644 0.5810644 0.5810649 0.5811048 0.5802067 0.04067370.6850063 0.7122076 0.7122076 0.7122076 0.7122076 0.7122076 0.7122076 0.7122076 0.7122084 0.7122695 0.712557 0.0419950.6920407 0.7855288 0.7855288 0.7855288 0.7855288 0.7855288 0.7855288 0.7855288 0.7855296 0.7855936 0.7863394 0.04282730.7035034 0.8815675 0.8815675 0.8815675 0.8815675 0.8815675 0.8815675 0.8815675 0.8815682 0.881621 0.8824202 0.04427390.7113028 0.9258567 0.9258567 0.9258567 0.9258567 0.9258567 0.9258567 0.9258568 0.9258572 0.9258971 0.9263707 0.04530590.7221758 0.9635033 0.9635033 0.9635033 0.9635033 0.9635033 0.9635033 0.9635033 0.9635035 0.963527 0.9634265 0.04678370.7334958 0.9832277 0.9832277 0.9832277 0.9832277 0.9832277 0.9832277 0.9832277 0.9832279 0.9832398 0.9826487 0.04834830.7417022 0.9905788 0.9905788 0.9905788 0.9905788 0.9905788 0.9905788 0.9905788 0.9905789 0.9905857 0.9897471 0.04949030.7507019 0.9950279 0.9950279 0.9950279 0.9950279 0.9950279 0.9950279 0.9950279 0.995028 0.9950312 0.9940093 0.05074560.7607625 0.9975769 0.9975769 0.9975769 0.9975769 0.9975769 0.9975769 0.9975769 0.997577 0.9975779 0.9964295 0.052150.7722304 0.9989351 0.9989351 0.9989351 0.9989351 0.9989351 0.9989351 0.9989351 0.9989351 0.9989346 0.9977063 0.05375010.785592 0.9995921 0.9995921 0.9995921 0.9995921 0.9995921 0.9995921 0.9995921 0.9995921 0.9995908 0.9983179 0.05561220.7931977 0.9997638 0.9997638 0.9997638 0.9997638 0.9997638 0.9997638 0.9997638 0.9997638 0.9997624 0.9984771 0.05667080.8011977 0.9998671 0.9998671 0.9998671 0.9998671 0.9998671 0.9998671 0.9998671 0.9998671 0.9998655 0.9985731 0.0577830.8171977 0.9999579 0.9999579 0.9999579 0.9999579 0.9999579 0.9999579 0.9999579 0.9999579 0.9999562 0.9986598 0.06000360.8251977 0.9999763 0.9999763 0.9999763 0.9999763 0.9999763 0.9999763 0.9999763 0.9999763 0.9999745 0.9986789 0.0611120.8331977 0.9999867 0.9999867 0.9999867 0.9999867 0.9999867 0.9999867 0.9999867 0.9999867 0.9999849 0.9986909 0.06221920.8411977 0.9999925 0.9999925 0.9999925 0.9999925 0.9999925 0.9999925 0.9999925 0.9999925 0.9999907 0.998699 0.0633250.8571977 0.9999976 0.9999976 0.9999976 0.9999976 0.9999976 0.9999976 0.9999976 0.9999976 0.9999958 0.9987096 0.06553270.8651977 0.9999987 0.9999987 0.9999987 0.9999987 0.9999987 0.9999987 0.9999987 0.9999987 0.9999968 0.9987136 0.06663460.8731977 0.9999992 0.9999992 0.9999992 0.9999992 0.9999992 0.9999992 0.9999992 0.9999992 0.9999974 0.9987172 0.06773520.8811977 0.9999996 0.9999996 0.9999996 0.9999996 0.9999996 0.9999996 0.9999996 0.9999996 0.9999978 0.9987206 0.06883450.8971977 0.9999999 0.9999999 0.9999999 0.9999999 0.9999999 0.9999999 0.9999999 0.9999999 0.9999981 0.9987271 0.07102920.9051977 0.9999999 0.9999999 0.9999999 0.9999999 0.9999999 0.9999999 0.9999999 0.9999999 0.9999981 0.9987303 0.07212470.9131977 1 1 1 1 1 1 1 1 0.9999982 0.9987334 0.07321880.9211977 1 1 1 1 1 1 1 1 0.9999982 0.9987365 0.07431170.9371977 1 1 1 1 1 1 1 1 0.9999982 0.9987427 0.07649350.9451977 1 1 1 1 1 1 1 1 0.9999982 0.9987457 0.07758250.9531977 1 1 1 1 1 1 1 1 0.9999982 0.9987488 0.07867020.9611977 1 1 1 1 1 1 1 1 0.9999982 0.9987518 0.0797566

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

0.9771977 1 1 1 1 1 1 1 1 0.9999982 0.9987579 0.08192570.9851977 1 1 1 1 1 1 1 1 0.9999982 0.9987609 0.08300830.9931977 1 1 1 1 1 1 1 1 0.9999982 0.9987639 0.0840896

1 1 1 1 1 1 1 1 1 0.9999982 0.9987664 0.085008

*Gráfica de T en función de Z y r

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

*Gráfica de X en función de Z y r

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

Grafico r vs T

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

Grafico r vs X

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC Grafico z vs <T>

Grafico z vs <X>

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN RADIAL

Universidad nacional del callao FIQ-UNAC

Cálculo del volumen del reactor tubular

*De la gráfica se obtuvo la longitud del reactor L:

Cálculo del volumen del catalizador

Por lo tanto la masa de l catalizador es:

BALANCE DE MATERIA Y ENERGIA EN UN REACTOR TUBULAR ADIABATICO DE LECHO FIJO CON DIFUSIÓN

RADIAL