Input Feedstock and Process Variables

To manipulate the feedstock information, we must drill down to the Reformer submodel. We enter the Reformer sub-model by clicking on Reformer Environment. 

File I Edit Simulation Flowsheet Reformer Tools Window Flelp 

Reactor Control Catalyst Product Heater Solver Options Solver Console Advanced Octane Curves EO Variables 

Feed Volume Flow [m9/h] Mass Flow [ka/hl Std. Vol Flow rm3/hl T empeiature C1 Pressure rkPal 

The full equation-oriented (EO) nature of the Reformer model technically allows us to enter the octane number of the product and back-calculate the required inlet temperatures to achieve the specified octane number. However, it is very unlikely that an uncalibrated model will converge with those specifications. We recommend entering reactor temperatures directly. 

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