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The base case simulation showed the value of key performance indicator that is mass ratio of acetone consumed to isophorone produced as 1.54.
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Compared with the base case simulation value of 4.59 wt% propylene yield, the maximized value shows an increase by 95%.
When it is compared with the base case simulation value of 4.59 wt% propylene yield, the maximized value shows an increase by 95%, as in case 1.
The results for both optimization cases 1, 2 and 3, and base case simulation (this simulation, Figs. 3, 4) are presented in Table 5, showing the riser exit values of the six lumps; gas oil as feed, while gasoline, butylene, propylene, dry gas and coke as products, and temperatures of the catalyst and gas phases.
A base case simulation was identified and established.
It compares the base case simulation results with the optimized cases 1, 2 and 3.
The base case simulation was run with a constant reservoir temperature of 22 °C.
This is a base case simulation with an initial load of 100,000 infecting bacterial cells in the target organ.
The base case is shown in Figure 1.
Simulation of the model for a base case shows that for a given output power, a more efficient system is bigger and vice versa.
The base-case simulations were compared to simulations for various auxiliary ventilation alternatives.
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