2022
DOI: 10.1016/j.petrol.2021.109615
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Simulation of the deasphalting process of crude oils: Models development and extraction conditions analysis

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Cited by 5 publications
(2 citation statements)
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“…Another deasphalting process is by solvent-based liquid–liquid extraction using light alkane solvents (C3–C6) to produce lightweight components removed from asphaltene. This operation usually occurs in temperatures from 100 to 150 °C. ,, The solvent-to-oil mass ratio used varies from 4 to 10, with the yield and quality of the oil obtained varying according to the heavy oil. The solvent used is one of the main factors that make this process expensive, and its recovery is essential for the economic viability …”
Section: Introductionmentioning
confidence: 99%
“…Another deasphalting process is by solvent-based liquid–liquid extraction using light alkane solvents (C3–C6) to produce lightweight components removed from asphaltene. This operation usually occurs in temperatures from 100 to 150 °C. ,, The solvent-to-oil mass ratio used varies from 4 to 10, with the yield and quality of the oil obtained varying according to the heavy oil. The solvent used is one of the main factors that make this process expensive, and its recovery is essential for the economic viability …”
Section: Introductionmentioning
confidence: 99%
“…In this study, SDA using n-heptane resulted in 25 wt% of asphaltenes removal. Heras et al [13] reported solvent deasphalting of crude oil using various solvents such as N-methyl-2-pyrrolidone, dimethylformamide, sulfolane, isopropanol, methanol, ethylene glycol, and ethyl acetate. It was found that methanol showed the highest asphaltene reduction efficiency of 84 wt% when the ratio of solvent to oil, and temperature were kept at 30 and 20 °C respectively.…”
Section: Introductionmentioning
confidence: 99%