Effectiveness of Different Transition Metal Dispersed Catalysts for In Situ Heavy Oil Upgrading

Ultradispersed particles of a size less than 100 nm for in situ catalytic upgrading have been reported to outperform the augmented catalytic upgrading achieved by incorporating pelleted refinery catalyst to the horizontal production well of the toe-to-heel air injection (THAI) process. Hydroconversion of heavy oil was carried out in a stirred batch reactor at 425 degrees C, 50 bar (initial H-2 pressure), 900 rpm, and 60 min reaction time using a range of unsupported transition metal (Mo, Ni, and Fe) catalysts. The effect of metal nanoparticles (NPs) was evaluated in terms of product distribution, physical properties, and product quality. The produced coke and recovered catalysts were also studied. The levels of API gravity and viscosity of the upgraded oils observed with the NPs was approximately 21 degrees API and 108 cP compared with thermal cracking alone (24 degrees API and 53.5 cP); this moderate upgrade with NPs is due to the lack of cracking functionality offered by supports such as zeolite, alumina, or silica. However, it was found that the presence of dispersed NPs significantly suppressed coke formation: 4.4 wt % (MoS2), 5.7 wt % (NiO), and 6.8 wt % (Fe2O3) compared to 12 wt % obtained with thermal cracking alone. The results also showed that with dispersed unsupported metal NPs in sulfide form the middle distillate (177-343 degrees C) of the upgraded oil was improved, particularly with MoS2, which gave SO wt % relative to 43 wt % (thermal cracking) and 28 wt % (feed oil). The middle distillate yields for Fe2O3 and NiO are 47 and 49 wt %, respectively. Hence, iron and nickel-based unsupported NPs showed similar activity when compared to the activity of MoS2. The cost and availability of iron-based catalysts compared to those of Ni and Mo for heavy oil upgrading are advantages that may justify its preference. Furthermore, the X-ray diffraction (XRD) and scanning electron microscopy (SEM) analyses showed that introducing dispersed catalysts to the upgrading helped to produce sponge-type coke that could be used as industrial fuel compared to shot-type obtained upon thermal cracking.