QUIMIOSTATO

V 1.9 Ltrs. SVt 1.52 Ltrs. S

Mo 0.0385 gr. XXo 0.0253 gr. X/L

µ 0.4592Ys/x 2.0008 gr. S/gr. X

µ max 0.6666Ks 0.005 gr. S/L

Cso 0.0385 gr. X/L

[X]=Xo*Exp(ut)

t (Hrs.) [X] g biomasa

0 0.0253 0.03850.5 0.0319 0.0484 0.0099 0.0199

1 0.0401 0.0609 0.0125 0.02501.5 0.0504 0.0767 0.0157 0.0315

2 0.0635 0.0965 0.0198 0.03962.5 0.0798 0.1213 0.0249 0.0498

3 0.1004 0.1527 0.0313 0.06273.5 0.1264 0.1921 0.0394 0.0788

4 0.1590 0.2416 0.0496 0.09924.5 0.2000 0.3040 0.0624 0.1248

5 0.2516 0.3825 0.0785 0.15705.5 0.3166 0.4812 0.0987 0.1975

6 0.3983 0.6054 0.1242 0.24856.5 0.5011 0.7616 0.1562 0.3126

7 0.6304 0.9582 0.1966 0.39337.5 0.7931 1.2055 0.2473 0.4948

8 0.9978 1.5167 0.3111 0.62258.5 0.9978 1.5167 0.0000 0.0000

9 0.9978 1.5167 0.0000 0.00009.5 0.9978 1.5167 0.0000 0.000010 0.9978 1.5167 0.0000 0.0000

10.5 0.9978 1.5167 0.0000 0.000011 0.9978 1.5167 0.0000 0.0000

h-1

h-1

al %10080 a)

3.53.4801 a) PERFIL:3.45513.42363.38403.33423.27163.19273.09362.96882.81182.61432.36582.05321.65991.16500.54250.54250.54250.54250.54250.54250.5425 b) CARGA TOTAL DE BIOMASA A LAS 7.5 HORAS:

M 7.5 1.2055 gr. X

0 2 4 6 8 10 120.0000

0.2000

0.4000

0.6000

0.8000

1.0000

1.2000

f(x) = 0.1144660032x - 0.1620657689R² = 0.9082795886

VARIACION DE LA [X]

TIEMPO (Hrs.)

CONCENTRACION DE BIOMASA

TURBIDOSTATO 6Hrs.

Xo 0.0000 gr. X /LF 0.6980 L/h b) Xo en la corriente de entrada:

D 0.4592Cso 3.5000 gr. S/ L BIOMASA: DXo-DX+µX=0

α

Yx/s 0.4998 Xo= 0.0000

El flujo es esteril.

D=µ= F/Vt

b) CARGA TOTAL DE BIOMASA A LAS 7.5 HORAS:

h-1

0 2 4 6 8 10 120.0000

0.2000

0.4000

0.6000

0.8000

1.0000

1.2000

f(x) = 0.1144660032x - 0.1620657689R² = 0.9082795886

VARIACION DE LA [X]

TIEMPO (Hrs.)

CONCENTRACION DE BIOMASA

2.2000 2.4000 2.6000 2.8000 3.0000 3.2000 3.4000 3.60000.0000

0.1000

0.2000

0.3000

0.4000

0.5000

0.6000

f(x) = - 0.1329854354x + 0.7901760274R² = 0.9880091058

Axis Title

Axis Title

b) Xo en la corriente de entrada:

α 0.3300 a α^2 0.5430b α 0.8096

α % 33.0038 c B 0.2655

α= Cso-Cs/Cso

Yx/s = 1 / Ys/x 0.65550.5766

d) Si Cso varia que pasa con el α

Cso α Cs

2.3658 0.4870 1.2138

e) si el flujo volumetrico aumenta un 50% cual sera la conversion de lactosa:

F 1.0470 a α^2 1.2049Vt 1.52 b α 1.4721D 0.6888 c B 0.2655

c) Cso= 3.5 gr.S / L porcentaje de conversion de lactosa (α) :

2.2000 2.4000 2.6000 2.8000 3.0000 3.2000 3.4000 3.60000.0000

0.1000

0.2000

0.3000

0.4000

0.5000

0.6000

f(x) = - 0.1329854354x + 0.7901760274R² = 0.9880091058

Axis Title

Axis Title

α 0.2199disminye la conversion del sustrato carbonado

f) perfil de conversion vs. Concentracion de sustrato

α Cs

0.3298 2.34570.3317 2.32580.3341 2.30080.3371 2.26940.3411 2.22980.3462 2.18010.3528 2.11750.3614 2.03870.3730 1.93980.3886 1.81520.4102 1.65850.4410 1.46150.4870 1.2138

0.32000.34000.36000.38000.40000.42000.44000.46000.48000.50000.0000

0.5000

1.0000

1.5000

2.0000

2.5000

f(x) = - 7.4149551148x + 4.7491286309R² = 0.9879381748

Perfil de la conversion vs. Cs

Axis Title

Axis Title

1.00001.4911

0.4890

I DCso α Cs

3.5000 0.3298 2.34573.4801 0.3317 2.32583.4551 0.3341 2.30083.4236 0.3371 2.26943.3840 0.3411 2.22983.3342 0.3462 2.18013.2716 0.3528 2.11753.1927 0.3614 2.03873.0936 0.3730 1.93982.9688 0.3886 1.81522.8118 0.4102 1.65852.6143 0.4410 1.46152.3658 0.4870 1.2138

e) si el flujo volumetrico aumenta un 50% cual sera la conversion de lactosa:

1.00001.22180.2203

2.2000 2.4000 2.6000 2.8000 3.0000 3.2000 3.4000 3.60000.0000

0.1000

0.2000

0.3000

0.4000

0.5000

0.6000

f(x) = - 0.1329854354x + 0.7901760274R² = 0.9880091058

Axis Title

Axis Title

0.32000.34000.36000.38000.40000.42000.44000.46000.48000.50000.0000

0.5000

1.0000

1.5000

2.0000

2.5000

f(x) = - 7.4149551148x + 4.7491286309R² = 0.9879381748

Perfil de la conversion vs. Cs

Axis Title

Axis Title

QUIMOSTATO TURBIDOSTATOXo 0.025 g/l F 0.8 l/h

µ 0.4592 D 0.5263V 1.52 l.Yx/s 0.4998 g.X/g.S α 0.4956µ max 0.6666 h-1Ks 0.005 g/lCsO 2 g/l

t, h X. g/l xO, g/l0 0.0250 0.0032

0.5 0.0315 0.00401 0.0396 0.0050

1.5 0.0498 0.00632 0.0626 0.0080

2.5 0.0788 0.01003 0.0991 0.0126

3.5 0.1247 0.01594 0.1569 0.0200

4.5 0.1974 0.02525 0.2484 0.0317

5.5 0.3125 0.0398 alfa6 0.3931 0.0501

6.5 0.4946 0.0631 α7 0.6222 0.0793

7.5 0.7828 0.09988 0.9848 0.1256

8.5 0.9849 0.12569 0.9848 0.1256

9.5 0.984910 0.9848

h-1 h-1

0 0.5 1 1.5 2 2.5 3 3.5 4 4.5 5 5.5 6 6.5 7 7.5 8 8.5 9 9.5 100.0000

0.2000

0.4000

0.6000

0.8000

1.0000

1.2000

X. g/l

0.4956

0.49562547

0 0.5 1 1.5 2 2.5 3 3.5 4 4.5 5 5.5 6 6.5 7 7.5 8 8.5 9 9.5 100.0000

0.2000

0.4000

0.6000

0.8000

1.0000

1.2000

X. g/l

0 0.5 1 1.5 2 2.5 3 3.5 4 4.5 5 5.5 6 6.5 7 7.5 8 8.5 9 9.5 100.0000

0.2000

0.4000

0.6000

0.8000

1.0000

1.2000

X. g/l