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BENZHYD - Dehydrogenation of Benzene

The gas-phase dehydrogenation of benzene to diphenyl (D) and further to triphenyl (T) is conducted in an ideal isothermal tubular reactor. The aim is to maximize the production of D and to minimize the formation of T. Two parallel, gas-phase reactions occur at atmospheric pressure [Pg.388]

The kinetics are given in terms of Arrhenius relationships and partial-pressure relationships as [Pg.389]

At steady-state conditions, the mass balance design equations for the ideal tubular reactor apply. These equations may be expressed as [Pg.389]

The ISIM program for this example with typical output is shown. Example BENZHYD [Pg.390]

Isothermal tubular reactor with two consecutive reactions [Pg.390]

5 Simulation Tools and Examples of Chemical Engineering Processes [Pg.374]

Study the effect of varying space time on the fractional conversions XI and X2 and evaluate the compositions of benzene, hydrogen, diphenyl and triphenyl. [Pg.375]


See other pages where BENZHYD - Dehydrogenation of Benzene is mentioned: [Pg.388]    [Pg.320]    [Pg.631]    [Pg.372]    [Pg.388]    [Pg.320]    [Pg.631]    [Pg.372]   


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Benzene dehydrogenation

Dehydrogenation of benzene

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