Catalytic cracking of heavy coker gas oil

Journal Article · Mon Jul 01 00:00:00 EDT 1985 · Chem. Technol. Fuels Oils (Engl. Transl.); (United States)

OSTI ID:5102565

Rustamov, M I; Farkhadova, G T; Farzullaev, T S; Guseinova, S B

The authors present results obtained in experiments on the catalytic cracking of heavy coker gas oil on a zeolitic catalyst, using as the catcracker feed either the original coker gas oil or this gas oil after dearomatization by furfural extraction. They conclude from an examination of their data that with the dearomatized feed the yield of butanebutylene cut is 20% higher, the yield of dry gas is lower by a factor of 1.6, and the yield of coke by a factor of 1.2. The characteristics of the naptha obtained by cracking original and dearomatized feeds indicate that the naptha obtained from cracking original gasoil contains 36% aromatics by weight, 10% more than that derived from the dearomatized feed.

• Research Organization: Inst. of Petrochemical Processes, Academy of Sciences of the Azerbaidzhan SSR
• OSTI ID: 5102565
• Journal Information: Chem. Technol. Fuels Oils (Engl. Transl.); (United States), Vol. 20:11; Other Information: Translated from Khimiya i Tekhnologiya Topliv i Maesl, No. 10, pp. 9-10, November, 1984
• Country of Publication: United States
• Language: English

Related Subjects

02 PETROLEUM
GAS OILS
CATALYTIC CRACKING
CATALYSTS
CHEMICAL REACTION YIELD
COKE
GAS YIELDS
NAPHTHA
VISCOSITY
ZEOLITES
CHEMICAL REACTIONS
COAL TAR OILS
CRACKING
DECOMPOSITION
DISTILLATES
ENERGY SOURCES
FOSSIL FUELS
FUELS
INORGANIC ION EXCHANGERS
ION EXCHANGE MATERIALS
MATERIALS
MINERALS
OILS
ORGANIC COMPOUNDS
OTHER ORGANIC COMPOUNDS
PETROLEUM
PETROLEUM DISTILLATES
PETROLEUM FRACTIONS
PETROLEUM PRODUCTS
PYROLYSIS
THERMOCHEMICAL PROCESSES
YIELDS
020400* - Petroleum- Processing