Trabajo De Aplicacion 2.xlsx

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Reactor CSTR

Ceo Cbo K R T

Ce 16.46 15.46 14.46 13.46 12.46 11.46 10.46 9.46 8.46 7.46 6.46 5.46 4.46 3.46 2.46 1.46 0.46

16.46 19.75 1.79E-04 8.314 673.15

τ 0 19.2217328 43.4176829 74.1420655 113.570278 164.814973 232.444977 323.370216 448.420083 625.314523 884.639167 1282.90733 1934.40757 3101.46424 5514.78241 12051.6939 51681.3894

Xe 0 0.06075334 0.12150668 0.18226002 0.24301337 0.30376671 0.36452005 0.42527339 0.48602673 0.54678007 0.60753341 0.66828676 0.7290401 0.78979344 0.85054678 0.91130012 0.97205346

Reactor CSTR 60000 50000 40000 30000 20000 10000 0

0

2

4

6

8

10

12

14

16

18

Reactor PFR

Ceo Cbo K R T

Ce 16.46 15.46 14.46 13.46 12.46 11.46 10.46 9.46 8.46 7.46 6.46 5.46 4.46 3.46 2.46 1.46 0.46

16.46 19.75 3.84E-04 8.314 673.15

τ 0 3.68317855 7.82830095 12.5284546 17.9036596 24.1114232 31.3627109 39.9469055 50.2723222 62.9350237 78.8423692 99.4507899 127.266588 167.038654 229.160758 342.799697 658.480451

Xe 0 0.06075334 0.12150668 0.18226002 0.24301337 0.30376671 0.36452005 0.42527339 0.48602673 0.54678007 0.60753341 0.66828676 0.7290401 0.78979344 0.85054678 0.91130012 0.97205346

Reactor PFR 700 600 500 400 300 200 100 0

0

2

4

6

8

10

12

14

16

18

Xe 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1

Volumen reactor PFR adiabatico (m3) 0 4.15656068235738E+022 4.28209927879075E+022 4.28589086043447E+022 4.28600537574509E+022 4.28600883439575E+022 4.28600893885571E+022 4.28600894201066E+022 4.28600894210595E+022 4.28600894210883E+022 4.28600894210891E+022

Volumen reactor PFR adiabatico (m3) 5E+022 4.5E+022 4E+022

Volumen (m3)

3.5E+022 3E+022 2.5E+022 2E+022 1.5E+022 1E+022 5E+021 0

0

0.1

0.2

0.3

0.4

0.5

0.6

Conversión de etanol

0.7

0.8

0.9

1

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