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The shell element as discussed in the previous section is used to model the reactor base and mat foundation.
In the model, the reactor is divided into three sections; devolatilization, volatile reactions and combustion-gasification.
In order to model the reactor, suitable thermodynamic, hydrodynamic and reaction models were solved simultaneously.
A 1.2 cm × 80 cm axi-symmetric model consisting of one entrance preheating fluid zone and a packed reaction zone was utilized to model the reactor.
Using this model, the reactor design is performed and key operational parameters are investigated in order to increase both H2 yield and H2/CO selectivity.
1D plug-flow, 2D boundary-layer and Navier Stokes, and 3D Navier Stokes equations are applied to model the reactor geometry.
Similar(53)
Using a mixed-integer nonlinear optimization (MINLP -based reactor synthesis MINLP -basedeactoreactorfurther optimized for maximizing CO2 utilization and synthesislectivity.
These two methods are illustrated by the dynamic simulation model of the reactor and/or by the pilot-plant reactor.
This paper presents the simulation model for the reactor with optimal geometry for pyrolysis of naphtha and biomass.
The controller synthesis follows the hierarchical structure previously proposed by the authors and uses the ASM1 model of the reactor and a standard model of the clarifier.
A simplified mass balance of the process is derived using a kinetic model for the reactor and black-box model for the separation section.
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model the unit
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example the reactor
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model the writer
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