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Mild hydrocracking of bitumen-derived coker and hydrocracker heavy gas oils; Kinetics, product yields, and product properties

Journal Article · · Industrial and Engineering Chemistry Research; (USA)
DOI:https://doi.org/10.1021/ie00093a002· OSTI ID:5241797
;  [1]
  1. Research Dept., Syncrude Canada Ltd., PO Box 5790, Edmonton, Alberta (CA)
The authors describe bitumen-derived coker and hydrocracker heavy gas oils hydrotreated at 350-400{sup 0}C, 7-11 MPa, 0.7-1.5h/sup -1/ LHSV, and 600 S m/sup 3/ of H/sub 2//m/sup 3/ of feed in a pilot-scale trickle-bed reactor, over presulfided commercial NiMo/Al/sub 2/O/sub 3/ catalysts. The conversion of HGO materials (343+ {sup 0}C) in feed to naphtha (195- {sup 0}C) and LGO (195/343 {sup 0}C) was determined by gas chromatographic simulated distillation. The degree of conversion was analyzed with modified first-order kinetics, which incorporate power terms for LHSV and hydrogen partial pressure. The equations were based on three cracking schemes; parallel, consecutive, and combined parallel-consecutive conversion.
OSTI ID:
5241797
Journal Information:
Industrial and Engineering Chemistry Research; (USA), Journal Name: Industrial and Engineering Chemistry Research; (USA) Vol. 28:9; ISSN IECRE; ISSN 0888-5885
Country of Publication:
United States
Language:
English

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