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Dynamics of a three-phase upflow fixed bed catalytic reactor

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Academic year: 2021

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Figure

Figure 1  T  TR 1 5 5 5 5 T T T T  TR PR  2  P  T  liquid  (CDT) N 2H28  T  3  7  6 T 9 4
Figure 2  Cooling oil (T M ) Liquid (TL)  Wall 2 (A 2 , T W2 )  Wall 1   (A 1 , T W1 )  Q 1 Q 3 Q 2 Q 1  = h 1  A 1  (T L  - T W1 ) Q2 = h2 A1 (TM - TW1 ) Q3 = h3 A2 (TM - TW2)
Figure 3  t = 10 mn 0102030405060708090100 0 0.25 0.5 0.75 1 1.25 1.5 Z (m)Concentrations (% mol) CDT_mod CDD_modCDE_modCDA_modCDT_expCDD_expCDE_expCDA_exp
Figure 4  t = 20 mn 0102030405060708090100 0 0.25 0.5 0.75 1 1.25 1.5 Z (m)Concentrations (% mol) CDT_mod CDD_modCDE_modCDA_modCDT_expCDD_expCDE_expCDA_exp
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