Thermal cracking of atmospheric residue versus vacuum residue

• Published in: Fuel processing technology Vol. 181; pp. 331 - 339
• Main Authors: Kaminski, Thomas, Husein, Maen M.
• Format: Journal Article
• Language: English
• Published: Amsterdam Elsevier B.V 01.12.2018; Elsevier Science Ltd
• Subjects: Asphaltene; Autoclaving; Catalyst; Catalysts; Catalytic cracking; Coke oven gas; Columns (process); Cracking; Drill cuttings; Gas oil; Gauges; Gravitation; LPG; Maltene; Mass balance; Simulation; Upgrading; Vacuum distillation; Asphaltene; AR; LPG; LGO; TI; Upgrading; Cracking; VR; Maltene; Catalyst; VGO; Drill cuttings
• ISSN: 0378-3820; 1873-7188
• DOI: 10.1016/j.fuproc.2018.10.014

Current practice subjects atmospheric residue (AR) to vacuum distillation, while feeding the vacuum residue (VR) for upgrading. This study explores the direct upgrading of AR and gauges the potential for eliminating the vacuum distillation unit, while recycling the upgraded oil to the atmospheric distillation column. Thermal cracking of Arabian AR and VR was carried out in an autoclave for 1 h at 400 °C. AR provided much higher liquid yield and quality with limited coke yield (<1 wt%). Higher temperature (420 °C) and longer residence time (2 h) were tested to further improve the quality of the liquid product. In addition, drill cuttings, previously demonstrated as an effective thermal cracking catalyst, were added to selected runs. Drill cuttings promoted the formation of short chain molecules, suppressed coke formation and significantly increased the quality of the product oil compared to control AR runs. Catalytic thermal cracking of AR at 420 °C for 2 h resulted in gas and coke yields of ~9 wt% and ~6 wt%, respectively, with the remainder being a premium quality liquid having °API gravity of 34. Upgrading of VR at the same conditions produced lower °API gravity liquid of 28 with 1.5 times more gas, 3 times more coke, and ~15 wt% less liquid yield. Simulated distillation showed that the product oil from both AR and VR upgrading contained ~20 wt% residue. Nevertheless, a mass balance of the whole refining/upgrading process revealed two times more liquified petroleum gas/light gas oil cut, with 50% less vacuum gas oil and 33% less coke yield for AR upgrading. [Display omitted] •A comparison between thermal cracking of AR and VR was carried out in an autoclave.•Thermal cracking of AR led to more liquid yield and less coke formation.•The liquid product from AR upgrading contributed to more light ends and less residue.•Drill cuttings promoted short chain hydrocarbon formation and reduced coke formation.