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In situ catalytic upgrading of heavy oil using a pelletized Ni-Mo/Al2O3 catalyst in the THAI process

机译:原位催化升级重油在泰式过程中使用粒化Ni-Mo / Al2O3催化剂

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Heavy oil and bitumen are difficult crudes to extract and upgrade, with additional transport and refining costs, because of their high viscosity, low API gravity, high asphaltenes, metals (V, Ni), and heteroatoms (N, S). Combining Toe-to-Heel Air Injection (THAI) with its catalytic add-on (CAPRI), a pelletized catalyst is incorporated along the outside of the horizontal producer well for in situ catalytic upgrading. This downhole upgrading process is one means to produce and partially upgrade heavy oil and bitumen with a reduced environmental footprint. In this study, the effectiveness of pelletized hydrodesulfurisation (HDS) Ni-Mo/Al2O3 catalyst for downhole catalytic upgrading was investigated at 350-425 degrees C, 20 bar, and 9h(-1) space velocity. The additional upgrading due to the presence of the catalyst was evaluated in terms of API gravity, viscosity, boiling point distribution, and sulfur and metals removals, before and after the experiment. The results indicate that the viscosity of the upgraded oil reduced by 1.7, 3 and 5 times less than the feed oil (0.49 Pa s) depending on the reaction temperature in the range 350-425 degrees C. The average increase in API gravity was approximately 2 to 5 while the gasoline yield showed an improvement of 2.5-13 wt.% above that of the original oil. There was also a modest reduction in the sulfur and metals (Ni + V) content of 2-8% and 1.3-9.2% (Ni + V), respectively. However, a possible limiting factor of the process was that rapid catalyst deactivation occurred due to coking.
机译:由于其高粘度,低API重力,高沥青质,金属(V,Ni)和杂原子(N,S),重油和沥青具有额外的运输和精炼成本,具有额外的运输和精炼成本。将Toe-to-Heel空气注射(泰国)与其催化加载(Capri)相结合,颗粒化催化剂沿水平生产者的外部掺入,用于原位催化升级。这种井下升级过程是一种生产和部分升级重油和沥青的一种方法,具有减少的环境足迹。在该研究中,在350-425℃,20巴和9h(-1)空速下研究了颗粒化加氢泡水合(HDS)Ni-Mo / Al 2 O 3催化剂的颗粒化加氢硫化(HDS)Ni-Mo / Al 2 O 3催化剂。根据API重力,粘度,沸点分布和硫和金属去除,在实验之前和之后评价导致催化剂存在的额外升级。结果表明,取决于350-425摄氏度范围内的反应温度,升级的油的粘度降低了1.7,3和5倍,这取决于反应温度的反应温度。API重力的平均增加约为2至5,而汽油产率显示出2.5-13重量%的增长。高于原油的%。硫和金属(Ni + v)含量的适度降低,分别为2-8%和1.3-9.2%(Ni + v)。然而,该方法的可能限制因素是由于焦化而发生快速催化剂失活。

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