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Effect of Hydrotreating Reaction Conditions on Viscosity, API Gravity and Specific Gravity of Maya Crude Oil

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Abstract

The hydrotreatment of Maya crude oil was carried out in a Parr batch reactor, using alumina-supported catalysts based on NiMo and CoMo sulfides, carbides, and nitrides, which were sulfided ex situ with a mixture of H\(_{2}\)/CS\(_{2}\), prior to reaction. Hydrotreating reactions were carried out under the following conditions: temperature: 320 \(^{\circ }\)C, pressure: 70–80 kg/cm\(^{2}\), time: 4 h, stirring: 500 rpm, and catalyst mass: 2 g. The products of reaction were analyzed by simulated distillation, and the physical properties of the hydrotreated crude were obtained, such as the specific weight and viscosity, at different temperatures, and these values were used to determine specific gravity (SG) and API. In this contribution, we illustrate changes in the physical properties of Maya crude oil before and after hydrotreatment reaction with variations on residue conversion when different hydrotreatment catalysts were used.

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References

  • Acevedo S, Escobar O, Echevarría L, Gutiérrez LB, Méndez B (2004) Structural analysis of soluble and insoluble fractions of asphaltenes isolated using the PNP method. relation between asphaltene structure and solubility. Energy Fuels 18:305–311

    Article  Google Scholar 

  • Ancheyta J, Rana MS, Furimsky E (2005) Hydroprocessing of heavy petroleum feeds: tutorial. Catal Today 109:3–15

    Article  Google Scholar 

  • Standard ASTM, D7169–11, 2005, (2011) Standard Test Method for Boiling Point Distribution of Samples with Residues Such as Crude Oils and Atmospheric and Vacuum Residues by High Temperature Gas Chromatography. ASTM International, West Conshohocken, PA 2011: doi:10.1520/D7169-11, http://www.astm.org

  • Dickenson RL, Biasca FE, Schulman BL, Johnson HE (1997) Refiners options for converting and utilizing heavy fuel oil. Hydrocarbon Process 76:57–62

    Google Scholar 

  • Dickie JP, Yen TF (1967) Macrostructures of the asphaltic fractions by various instrumental methods. Anal Chem 39:1847–1852

    Article  Google Scholar 

  • Jacquin Y, Toulhoat H, Quignard A, Le Page JF (1983) Développements récents dans le domaine de l’hydrotraitement des fractions lourdes. Oil Gas Sci Technol - Rev. IFP 38:371–385

    Google Scholar 

  • Peries JP, Renard P, Des Courires T, Rossarie J (1988) ASVAHL new routes for processing heavy oils. In: Proceedings of the 4th UNITAR/UNDP International Conference on Heavy Crude and Tar Sands, Edmonton, Canada, Aug. 18, 1988; paper 95, pp 1–21

    Google Scholar 

  • Rana MS, Sámano V, Ancheyta J, Díaz JA (2007) A review of recent advances on process technologies for upgrading of heavy oils and residua. Fuel 86:1216–1231

    Article  Google Scholar 

  • Shuetze B, Hoffman H (1984) How to upgrade heavy feeds. Hydrocarbon Process 2:75–82

    Google Scholar 

  • Speight JG (1999) The chemistry and technology of petroleum. Marcel Dekker, New York

    Book  Google Scholar 

  • Tynan EC, Yen TF (1969) Association of vanadium chelates in petroleum asphaltenes as studied by ESR. Fuel 43:191–208

    Google Scholar 

  • Villasana Y, Luis-Luis MA, Labrador H, Brito JL (2011) Optimización del tiempo de reacción de hidrotratamiento del crudo Furrial usando como catalizador \(\text{ NiMo }/\gamma -{\rm {Al}}_{2}{\rm {O}}_{3}\) In: Barbosa AL, Villa AL, Ramírez A (eds) VII Simposio Colombiano de Catálisis (ISBN: 978-958-8736-16-7) Editorial Universidad de Cartagena. Cartagena de Indias. Paper N\(^\circ \) CA-P0-5

    Google Scholar 

  • Villasana Y, Ruscio-Vanalesti F, Pfaff C, Méndez FJ, Luis-Luis MA, Brito JL (2013a) Atomic ratio effect on catalytic performance of FeW-based carbides and nitrides on thiophene hydrodesulfurization. Fuel 110:259–267

    Article  Google Scholar 

  • Villasana Y, Escalante Y, Rodríguez-Nuñez JE, Méndez FJ, Ramírez S, Luis-Luis MA, Ancheyta J, Brito JL (2013b) Maya crude oil hydrotreating reaction in a batch reactor using NiMo carbide and nitride as catalysts. Catalysis Today, submitted

    Google Scholar 

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Acknowledgments

One of us (Y. V.) acknowledges financial support from FONACIT and IVIC. We also thank E. Rodriguez, A. Quitian, G. Felix, R. Rivera, J. Antonio Montes, F. Hernández, and F. Alonso for experimental, technical, and analysis support.

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Correspondence to Yanet Villasana .

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Villasana, Y., Ramírez, S., Ancheyta, J., Brito, J.L. (2014). Effect of Hydrotreating Reaction Conditions on Viscosity, API Gravity and Specific Gravity of Maya Crude Oil. In: Sigalotti, L., Klapp, J., Sira, E. (eds) Computational and Experimental Fluid Mechanics with Applications to Physics, Engineering and the Environment. Environmental Science and Engineering(). Springer, Cham. https://doi.org/10.1007/978-3-319-00191-3_28

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