Molecular transformation of Athabasca bitumen end-cuts during coking and hydrocracking

• Published in: Fuel (Guildford) Vol. 80; no. 8; pp. 1155 - 1163
• Main Authors: Zhao, S., Kotlyar, L.S., Woods, J.R., Sparks, B.D., Hardacre, K., Chung, K.H.
• Format: Journal Article Conference Proceeding
• Language: English
• Published: Oxford Elsevier Ltd 01.06.2001; Elsevier
• Subjects: Applied sciences; Bitumen pitch; Coking; Crude oil, natural gas and petroleum products; End-cut; Energy; Exact sciences and technology; Fuels; Hydrocracking; Molecular transformation; Processing of crude oil and oils from shales and tar sands. Processes. Equipment. Refinery and treatment units; Coking; Molecular transformation; Bitumen pitch; End-cut; Hydrocracking; Chemical transformation; Upgrading; Chemical structure; Athabasca deposit; Supercritical solvent; Chemical decomposition; Solvent extraction; Bitumen; Tar sand
• ISSN: 0016-2361; 1873-7153
• DOI: 10.1016/S0016-2361(00)00180-0

The use of supercritical pentane, under increasingly severe conditions of temperature and pressure, allows residual oils to be separated into fractions with progressively higher molecular weight without significant chemical degradation. Characterisation of these individual fractions provides a more complete picture of bitumen resid chemistry than average values determined for the whole sample. In the work described here, this approach has been applied to resid samples taken from the bitumen upgrading units at the Syncrude Canada Ltd. plant in Northern Alberta (Oil Gas J, 20 (1997) 66; Rev Process Chem Engng, 1 (1998) 41). A significant amount of each sample was non-extractable under even the most severe conditions. These end-cuts from virgin bitumen pitch (P-EC), hydrocracking product resid (HC-EC) and coking product resid (CK-EC) were compared to pentane insoluble asphaltenes (ASP) from a conventional coker feed bitumen. In addition, the P-EC sample was subjected to further fractionation based on its solubility in different blends of toluene and pentane. The P-EC sample comprises about 55%(w/w) highly aromatic heavy molecules, rich in heteroatoms and metals. Smaller molecules, with much lower aromaticity and polarity, represent the remaining 45%(w/w). Owing to a their high heteroatom and metals content, the heavier molecules in this material are considered to be major coke precursors under thermal cracking conditions. However, in hydrocracking the free radicals generated by the cleavage of carbon–carbon and sulphur–carbon bonds are suppressed by hydrogen capping. As a result, the “difficult to crack” aromatic “cores” of the heavier components remain toluene soluble. Although these components do not form coke under hydrocracking conditions, they may cause fast catalyst deactivation. In existing commercial processes the residue from hydrocracking is recycled to extinction in a coker. Because of its intractable nature, this heavy resid may not be conducive to the production of lighter liquid products. It is suggested that, prior to hydrocracking, the heaviest portion of bitumen pitch be removed to avoid these problems.