Dynamic Simulation of an Isobaric Nonisothermal HDT Commercial Reactor

2 Dynamic Simulation of an Isobaric Nonisothermal HDT Commercial Reactor 

The three-phase nonisothermal reactor model was used to simulate the performance of a commercial reactor. The model solution for this case also becomes an 

FIGURE 7.17 (a) Profiles of dynamic sulfur concentration and (b) temperature as a function of time on (—) commercial reactor (z = 853.44cm = 0.72cm/s Uq = 8.93cm/s), (—) 

Modeling of Processes and Reactors for Upgrading of Heavy Petroleum 

FIGURE 7.18 Dynamic sulfur concentration profiles in the liquid phase of commercial 

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