Increasing the flash point temperature of DCO oil products to meet the FO (FP) baseline standard of Dung Quat refinery

  • Nguyen Hoang Tri Binh Son Refining and Petrochemical JSC
  • Nguyen Chanh Quoc Binh Son Refining and Petrochemical JSC
  • Huynh Cong Vinh Binh Son Refining and Petrochemical JSC
  • Bui Anh Khanh Binh Son Refining and Petrochemical JSC
  • Ho Quang Xuan Nhan Binh Son Refining and Petrochemical JSC
  • Nguyen Huu Trung Binh Son Refining and Petrochemical JSC
  • Bui Van Vuot Binh Son Refining and Petrochemical JSC
  • Nguyen Thanh Bong Binh Son Refining and Petrochemical JSC
Keywords: DCO, flash point (FP), stripping, BSR, fuel oil, result, light component

Abstract

The flash point temperature of decanted oil (DCO) has been consistently low since the Dung Quat refinery commenced operations in 2009. This issue is attributed to the absorption of trace amounts of light gases such as H2, CH4, and C2H6 by the liquid stream at the bottom of the tower. These gases cannot be effectively separated through distillation at T-1501, and neither modifications to hardware nor adjustments to the angle of the fifth packing layer have proven effective. The separation of these light gases can only be achieved by applying the stripping method to the DCO product stream emanating from the bottom of the tower and at D-1515. This method must ensure no alterations to existing hardware and utilize current equipment solely. The technique involves injecting N2 directly into the liquid drum to remove light gases by reducing the partial pressure of hydrocarbons. This solution successfully increased the DCO flash point temperature from 49°C to 84°C in July 2018, and has been maintained to date. Furthermore, the flash point temperature can be regulated by the N2 stream to exceed 100°C, thereby meeting and surpassing the technical requirement of 66°C.

References

Norman P. Lieberman, and Elizabeth T. Lieberman, A working guide to process equipment. McGraw-Hill, 2014.
Reza Sadeghbeigi, Fluid catalytic cracking handbook. Butterworth-Heinemann, 2019.
Published
2025-12-22
How to Cite
Nguyen , H. T., Nguyen, C. Q., Huynh, C. V., Bui, A. K., Ho , Q. X. N., Nguyen , H. T., Bui , V. V., & Nguyen, T. B. (2025). Increasing the flash point temperature of DCO oil products to meet the FO (FP) baseline standard of Dung Quat refinery . Petrovietnam Journal, 6, 55-60. https://doi.org/10.47800/PVSI.2025.06-06