Taller De Reactores Final.xlsx
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umax
So
Ks
0.5
Yx/s
10
Xo
0.1
t
0.5
u
0.1
0 0.4950495 2 4 6 8 10 12 14 16
X vs t 300 250
X
200 150 100 50 0
0
2
4
6
8 tiempo
10
12
14
16
18
X
log(X)
0.1 0.26915009 0.72441773 1.94977101 5.24781052 14.124487 38.0160701 102.320288 275.395153
-1 -0.5700055 -0.1400109 0.28998361 0.71997815 1.14997268 1.57996722 2.00996176 2.43995629
Log(X)
Log(X) vs t 3 2.5 2 1.5 1 0.5 0 0 -0.5 -1 -1.5
2
4
6
8
10
t
12
14
16
18
F(L/h)
X(g/L)
S(g/L)
1 1.4 1.6 1.7 1.8 1.9
3.15 3.22 3.27 3.26 3.21 3.1
Volumen
Disolucion=u(1/h)
0.01 0.038 0.071 0.066 0.095 0.477
2
Sinicial
0.5 0.7 0.8 0.85 0.9 0.95
10
0.6
3.3
0.5
3.25
0.4
3.2
0.3
3.15
0.2
3.1
0.1
3.05
0 0.4
0.5
0.6
0.7
0.8
0.9
1
2.5 2
f(x) = 0.0095 R² = 0.96644
1.5
Sustrato Biomasa
1/u
Concentracion(kg/L)
punto b: X vs S
1 0.5
3
0
0
20
Velocidad de dilucion
Yxs 1/Yxs 1/D 0.31531532 3.17142857 2 0.32322827 3.09378882 1.42857143 0.3293383 3.03639144 1.25 0.32816589 3.04723926 1.17647059 0.32407875 3.08566978 1.11111111 0.32552767 3.07193548 1.05263158
1/Yxs VS 1/D 3.2 3.15
f(x) = 0.1173542006x + 2.9275692148 R² = 0.7340174982
3.1 3.05 3 2.95
1
1.2
1.4
1.6
1.8
2
2.2
u
Lineweaver-Burk 1/s 1/u 0.5 100 2 0.7 26.3157895 1.42857143 0.8 14.084507 1.25 0.85 15.1515152 1.17647059 0.9 10.5263158 1.11111111 0.95 2.09643606 1.05263158
Edie Hofstee u 0.5 0.7 0.8 0.85 0.9 0.95
Edie Hofstee
Lineweaver-Burk 60
2.5
50
2
f(x) = 0.0095322729x + 1.0692831462 R² = 0.9664424826
1
10 0
20
40
60
80
Estequiometrico pendiente intercepto Yxs Ms
2.2
100
120
0 0.4
0.5
0.6
0.7 u
1/S
2
30 20
0.5 0
f(x) = - 99.1363217472x R² = 0.921472957
40 u/s
1/u
1.5
0.1174 2.9276 0.34157672 0.1174
0.5
Edie Hofstee u/s
s
50 18.4210526 11.2676056 12.8787879 9.47368421 1.99161426
Lagmuir s/u 0.01 0.02 0.038 0.05428571 0.071 0.08875 0.066 0.07764706 0.095 0.10555556 0.477 0.50210526
Pendiente Intercepto µmax Ks
Lagmuir
Edie Hofstee
0.6 0.5
f(x) = 1.0276424262x + 0.0117363792 R² = 0.9996830234
0.4
S/U
f(x) = - 99.1363217472x + 94.9955761371 R² = 0.921472957
0.3 0.2 0.1
0.6
0.7 u
0.8
0.9
1
0 0
0.1
0.2
0.3
S
0.4
0.5
0.6
1.0276 0.0117 0.9731413 0.01138575
92
0.4
0.5
0.6
So
Ks
0.5
Yx/s
10
Xo
0.1
t
0.5
u
0.1
0 0.4950495 2 4 6 8 10 12 14 16
X vs t 300 250
X
200 150 100 50 0
0
2
4
6
8 tiempo
10
12
14
16
18
X
log(X)
0.1 0.26915009 0.72441773 1.94977101 5.24781052 14.124487 38.0160701 102.320288 275.395153
-1 -0.5700055 -0.1400109 0.28998361 0.71997815 1.14997268 1.57996722 2.00996176 2.43995629
Log(X)
Log(X) vs t 3 2.5 2 1.5 1 0.5 0 0 -0.5 -1 -1.5
2
4
6
8
10
t
12
14
16
18
F(L/h)
X(g/L)
S(g/L)
1 1.4 1.6 1.7 1.8 1.9
3.15 3.22 3.27 3.26 3.21 3.1
Volumen
Disolucion=u(1/h)
0.01 0.038 0.071 0.066 0.095 0.477
2
Sinicial
0.5 0.7 0.8 0.85 0.9 0.95
10
0.6
3.3
0.5
3.25
0.4
3.2
0.3
3.15
0.2
3.1
0.1
3.05
0 0.4
0.5
0.6
0.7
0.8
0.9
1
2.5 2
f(x) = 0.0095 R² = 0.96644
1.5
Sustrato Biomasa
1/u
Concentracion(kg/L)
punto b: X vs S
1 0.5
3
0
0
20
Velocidad de dilucion
Yxs 1/Yxs 1/D 0.31531532 3.17142857 2 0.32322827 3.09378882 1.42857143 0.3293383 3.03639144 1.25 0.32816589 3.04723926 1.17647059 0.32407875 3.08566978 1.11111111 0.32552767 3.07193548 1.05263158
1/Yxs VS 1/D 3.2 3.15
f(x) = 0.1173542006x + 2.9275692148 R² = 0.7340174982
3.1 3.05 3 2.95
1
1.2
1.4
1.6
1.8
2
2.2
u
Lineweaver-Burk 1/s 1/u 0.5 100 2 0.7 26.3157895 1.42857143 0.8 14.084507 1.25 0.85 15.1515152 1.17647059 0.9 10.5263158 1.11111111 0.95 2.09643606 1.05263158
Edie Hofstee u 0.5 0.7 0.8 0.85 0.9 0.95
Edie Hofstee
Lineweaver-Burk 60
2.5
50
2
f(x) = 0.0095322729x + 1.0692831462 R² = 0.9664424826
1
10 0
20
40
60
80
Estequiometrico pendiente intercepto Yxs Ms
2.2
100
120
0 0.4
0.5
0.6
0.7 u
1/S
2
30 20
0.5 0
f(x) = - 99.1363217472x R² = 0.921472957
40 u/s
1/u
1.5
0.1174 2.9276 0.34157672 0.1174
0.5
Edie Hofstee u/s
s
50 18.4210526 11.2676056 12.8787879 9.47368421 1.99161426
Lagmuir s/u 0.01 0.02 0.038 0.05428571 0.071 0.08875 0.066 0.07764706 0.095 0.10555556 0.477 0.50210526
Pendiente Intercepto µmax Ks
Lagmuir
Edie Hofstee
0.6 0.5
f(x) = 1.0276424262x + 0.0117363792 R² = 0.9996830234
0.4
S/U
f(x) = - 99.1363217472x + 94.9955761371 R² = 0.921472957
0.3 0.2 0.1
0.6
0.7 u
0.8
0.9
1
0 0
0.1
0.2
0.3
S
0.4
0.5
0.6
1.0276 0.0117 0.9731413 0.01138575
92
0.4
0.5
0.6
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