In this work, physical modeling of thermal steam treatment of high viscosity oil without and with the addition of a suspended catalyst to the system was performed. The aim of the magnetite effect for the in- situ upgrading in the production of high viscosity oils was to reduce the content of asphalt-resinous compounds and their molecular weight, while significantly increasing the content of saturated and aromatic hydrocarbons. The presence of a catalyst promoted decarboxylation reactions, as indicated by the significant amount of carbon dioxide produced as the catalyst concentration increased. In addition, the produced carbon dioxide decreased the viscosity of the oil and improved the chemical composition of the group. The introduction of a hydrogen donor helped to reduce the formation of aromatic hydrocarbons in the gas phase composition and prevented the polymerization of the produced hydrocarbons. The determination of viscosity-temperature characteristics showed a significant decrease in the viscosity of the obtained products after the catalytic aquathermolysis of oil. Indeed, during the catalytic aquathermolysis, maghemite was reduced to magnetite by the interaction of iron oxide with steam. In parallel, in the presence of a catalyst, with increasing exposure temperature, the content of hydrogen sulfide was reduced and the formation of iron sulfides such as pyrrhotite was observed.
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