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- W2091718382 abstract "A mathematical model is presented for simulating the steady-state catalytic dehydrogenation of ethylbenzene to styrene and other associated side reactions. The various differential equations describing the material and energy balances were integrated using a fourth-order Runge-Kutta method on an IBM 7090. Several runs on the computer were made to study the effect of change in feed rates, feed-to-steam ratio, and inlet temperature and pressure, on styrene yield. It is shown how, with the computer results, a profit equation for a particular plant may be derived for possible use in on-line optimization and control." @default.
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- W2091718382 date "1965-09-01" @default.
- W2091718382 modified "2023-09-26" @default.
- W2091718382 title "Simulation of the Catalytic Cracking Process for Styrene Production" @default.
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- W2091718382 doi "https://doi.org/10.1147/rd.95.0388" @default.
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