Conclusions
To optimize the process it is necessary:
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1.
To keep the octane number of the stabilized product at the lower limit N=72.
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2.
To maintain the temperature T at the highest admissible level T=503°C.
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3.
To calculate the feed rate of the starting material G as a function of T and yN+yA from the condition of maximum net return. It is convenient to restrict G after the process has been optimized.
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4.
To increase the mass flow rate G as the quality of the starting material improves (yA+yN rises), and vice versa.
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Literature cited
B. A. Bel'tsov, Khim. i tekhnol. topliv i masel, No. 8 (1966).
D. Ya. Andreev and B. A. Bel'tsov, Khim. i tekhnol. topliv i masel, No. 5 (1966).
S. Gass, Linear Programming [in Russian], Izd. Fizmatgiz (1961).
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Translated from Khimiya i Tekhnologiya Topliv i Masel, No. 4, pp. 31–32, April, 1967.
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Bel'tsov, B.A. Algorithm suitable for steering the platforming process. Chem Technol Fuels Oils 3, 259–261 (1967). https://doi.org/10.1007/BF00731748
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DOI: https://doi.org/10.1007/BF00731748