الفهرس 
Theoretical BackgroundOnly 14 pages are availabe for public view
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Abstract
analysis has been carried out and kinetic model for catalytic reforming based on ’••oftemperature (at low pressure.) on the rate of conversion on the four major reactions has been studied.
’on ofnaphthenes to aromatics
ion of paraffms to naphthenes & ( decyclization of naphthenes to paraffins)
king of paraffins
. g of naphthenes
of temperature and equilibrium constants on the rate of reaction has been studied .,cases,
. show good agreement and increases in rate of conversion with increasing in
in both method, except for decyclization of naphthenes to paraffms where shows that such reaction may occur below 400°C ,and within the range of
conditions for commercial CCR platforming [450°C - 550°C] the increases in is in favour of the reverse reaction ( dehydrocyclization of paraffins to
).
sed model was based on Garimella reaction network and corresponding rate .. using the global material and energy balance equations for radial flow reactor, was applied on 3 different platforming reactions for each reactor.
’ng plant data has been applied.
18 show good agreement with CCR platforming reactor profiles.