THERMOCATALYTIC CONVERSION PROCESS OF HEAVY GASOIL OF CATALYTIC CRACKING AND ITS MIXTURE WITH COTTONSEED OIL
The production process of (C2–C4) low molecular weight olefins as a result of thermocatalytic conversion of the fraction heavy gasoil of catalytic cracking (HGCC) and its mixture with cottonseed oil in the temperature range of 550–7000C has been investigated. It is faund that at result the thermocatalytic conversion of pure HGCC fraction at 7000C, the increase of 16.1–16.4 and 6.3–6.1% have been recorded for the yield of ethylene and propylene respectively. When 10% of cottonseed oil is added to this fraction in the presence of Omnikat-210P and Omnikat-210P/halloysite mixture catalysts in 7000C, 3–2.8 and 0.6–1.4% of mass increases have been observed for ethylene and propylene respectively.
Keywords : catalytic cracking, heavy gasoil, ethylene, propylene, halloysite, low molecular weight olefins
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