Modified design for vacuum residue processing

  • Sandro-Faruc González Ecopetrol – Instituto Colombiano del Petróleo, Piedecuesta, Colombia
  • Jesus Carrillo Ecopetrol – Instituto Colombiano del Petróleo, Piedecuesta, Colombia
  • Manuel Núñez Ecopetrol – Instituto Colombiano del Petróleo, Piedecuesta, Colombia
  • Luis-Javier Hoyos Ecopetrol – Instituto Colombiano del Petróleo, Piedecuesta, Colombia
  • Sonia-A. Giraldo Universidad Industrial de Santander, Bucaramanga, Colombia
Keywords: Visbreaking, Demex, Hydrotreating, Vacuum residues, Light gas oil

Abstract

The world petroleum industry shows a decreasing in the oil reserves, specially the light kind. For this reason is very important to implement process schemes that give the possibility to improve the recuperation of valuable products of heavy oil. In this case the bottom processing in each one of the petroleum refining stages earns great importance with the purpose of maximizing the quantity of fuel by barrel of raw processed. Therefore, it has been proposed the modification of the currently vacuum residues process scheme in the Ecopetrol`s Barrancabermeja refinery (DEMEX-Visbreaking-Hydroprocessing). That modification consists in the incorporation of an additional Visbreaking stage, previous at DEMEX extraction stage.

This investigation was developed with plant pilot tests combined with statistical models that predict the yield and the quality of the products obtained in the industrial plants. These models were developed by the Instituto Colombiano de Petróleo (ICP).

The modified scheme Visbreaking I-DEMEX- Visbreaking II- Hydroprocessing, gives the possibility to increase the yield of middle distillates. Besides decrease the quantity of demetalized oil produced in DEMEX stage. This reduction is very favorable since environmental point of view, because it allows have a percentage of free capacity in the Hydroprocessing unit in order to removed sulfur of valuable products like Diesel and in this way to respect the environment law to this kind of fuel.

References

Bonilla, J. & Meyers, R. (1986). Handbook of petroleum refining processes. Ed. McGraw Hill: 8: 8-35. New York.

Cabrera, C. & Meyers, R. (1986). Handbook of petroleum refining processes. Ed. McGraw Hill: 6 :6-23. New York.

Celestino, J. & Hernández, R. (1982). Processes compared for upping maya distillate yield. Oil & Gas J., 80(16): p 111-115.

Di Carlo, S. & Janis, B. (1992). Composition and Visbreakability for Petroleum Residues. Chem. Eng. Sci., 47, 2675-2670.

Ditman, J. & Van Hook, D.(1981). Upgrading of residual oils by solvent deasphalting and delayed coking. ACS meeting, Atlanta, USA.

Fainberg, V., Podorozhasky, M., Hetsroni, G., Brauch, R. & Kalchouck H. (1996). Changes in the Composition and properties of the vacuum residues as a result of visbreaking. Fuel Sci Technol. Int. 14, 839-845.

Raseev, S. (2003). Thermal Processes in petroleum refining. Ed. Marcel Decker Inc: 119-120. New York

Salazar, J. & Meyers, R. (1986). Handbook of petroleum refining processes. Ed. McGraw Hill.; p.7-66. New York

Sumbogo, S., Yang, H., Choi, K., Korai, Y. & Mochida, I. (2003). Influences of nitrogen species on the hydrodesulfurization reactivity of a gas oil over sulfide catalysts of variable activity. Appl. Catal. A., 252, 331-346.
How to Cite
González, S.-F., Carrillo , J., Núñez , M., Hoyos, L.-J., & Giraldo, S.-A. (2020). Modified design for vacuum residue processing. CT&F - Ciencia, Tecnología Y Futuro, 4(2), 57-69. Retrieved from https://ctyf.journal.ecopetrol.com.co/index.php/ctyf/article/view/245

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Published
2020-04-15
Section
Scientific and Technological Research Articles

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