Treating Wet Oil in Amara Oil Field Using Nanomaterial (SiO2) With Different Types of De emulsifiers

Authors

  • Ayat Ragheb Alkarbalaee Department of Petroleum Technology, College of Engineering, University of Technology, Iraq
  • Adel Sharif Hammadi Department of Chemical Engineering, College of Engineering, University of Technology, Iraq
  • Ghassan Hamid Abdul Majeed Research and Development Department, Ministry of Higher Education and Scientific Research, Baghdad, Iraq

DOI:

https://doi.org/10.31699/IJCPE.2021.1.4

Keywords:

emulsion, demulsifies, crude oil, saltwater, (w/o)emulsion, nanomaterial

Abstract

One of the most important problems in the oil production process and when its continuous flow, is emulsified oil (w/o emulsion), which in turn causes many problems, from the production line to the extended pipelines that are then transported to the oil refining process. It was observed that the nanomaterial (SiO2) supported the separation process by adding it to the emulsion sample and showed a high separation rate with the demulsifiers (RB6000) and (sebamax) where the percentage of separation was greater than (90 and 80 )%  respectively, and less than that when dealing with (Sodium dodecyl sulfate and Diethylene glycol), the percentage of separation was (60% and 50%) respectively.

   The high proportion of (NaCl + distilled water) raises the probability of the separation efficiency as the separation was (88.5,79)% and (65.5, 55) %  for (RB6000, SebaMax)respectively with (SiO2) at 70 °C, while the results of separation were (77,85)% and (65,40)  for (RB6000, Seba Max) respectively with (SiO2) at 50 °C after 120 minutes, where the (w/o ratio) was (9:1) for the high separation results and (7:3) for the lower separation results, at a speed of (12000rpm), and with a salt concentration of (1500) ppm, and less of these results at lower volumetric and temporal conditions. The (NaCl) salt deals with the wall films separating the droplets and reduces their viscosity [1].

   As for the pH factor, it is at the value (2 and 3) represent a stable emulsion that is difficult to separate easily, but with the passage of raising the pH away from the acidic medium and near to the basic direction, a significant increase in the separation process was observed compared with the acidic medium at lower values, after 120 minutes the separation seemed to be good efficient, reaching (60 and 70) % respectively, while at the same time the emulsion reached a more efficient separation level with a pH of (  8 and 7) equal to (80 and 87.3)  %, at 50 °C with SebaMax demulsifier in presence of (SiO2), and with the same pH values, an increase was observed in the separation with the increase in temperature to (70 °C), then it returns to be a reverse emulsifier when the value exceeds (10) to (11, 12, 13).

References

A. Al-Alawy and M. Al-Ameri, “Treatment of Simulated Oily Wastewater by Ultrafiltration and Nanofiltration Processes”, ijcpe, vol. 18, no. 1, pp. 71-85, Mar. 2017.

Ajay Mandal, Achinta Bera, "Modeling of flow of oil-in-water emulsions through porous media", journal of petroleum science and technology,Vol.12No2(April 2015)

Troner A.de Souzaa , Agnes de P.Scheera , MárciaCristina Khalilb, Carlos I. Yamamotoa, Luiz Fernando de L.LuzJr.a , "Emulsion inversion using solid particles" , Journal of Petroleum Science and Engineering ,V. 96–97, October 2012. Pages 49-57

Kadhem Hammoud Manati ; (Report about Amara Gas Separation Plant), Maysan Oil Company (MOC), Operations Authority (Production and Discharge Authority), Petroleum Engineering Department (2018).

Bhardwaj, A. and Hartland, S, "Studies on Build up of Interfacial Film at the Crude Oil/Water Interface", Journal of Dispersion Science and Technology, Vol 19. No.4,pages 465-473, (1998).

Selvarajan Radhakrisnan, Anantha-subramaniam Sivakumar , Robert A. M, " Aqueous Dispersion of an oil Soluble demulsifier for breaking Crude Oil Emulsions", US Patent , No.6, pages 294,093,(2001).

Swastic and das, S. ,"Effect of different acids on the scale in pipelines of Linz-Donawitz (LD) Plant (Steel Making Process)" ,. Advances in Chemical Engineering and Science,No5, pages 192-196, (2015).

Siew fan wong,J.s.lim , Sharul sham dol," Crude oil emulsion: A review on formation, classification and stability of water-in-oil emulsions", journal of petroleum science and Engineering Vol.135,Nov.2015,pp 498-504.

A. Saniere, I. Hénaut, J.F. Argillier," Pipeline Transportation of Heavy Oils a Strategic, Economic and Technological Challenge", Oil & Gas Science and Technology - Rev. IFP, Vol. 59No.5 (2004), pp. 455-466

F. H. Wang, L. B. Shen, H. Zhu, K. F. Han, " The Preparation of a Polyether Demulsifier Modified by Nano-SiO2 and the Effect on Asphaltenes and Resins", Petroleum Science and Technology, Vol.29No24, (25-Oct,2011), pp2521-2529

D. M. Pinchao, C. A. Cedeño, F. B. Cortés, C. A. Franco, "Water/oil emulsions separation using SiO2 nanoparticles/surfactant-based nanofluids" , Universidad Nacional de Colombia , Acipet journal, 2015.

Hemmingston, P.V., Silset, A., Hannisdal, A., Sjöblom, J; " Emulsions of heavy crude oils I: influence of viscosity, temperature and dilution"; . J. Disp. Sci. Technol. 2005. 26, 615–627.

Jones, T.J., Neustadter, E.L., and Wittingham, K.P., “Water-in-Crude Oil Emulsion Stability and Emulsion Destabilization by Chemical Demulsifiers”, J. Petrol. Can. Technol., pp 100-108, April-June (1978).

Sunil Lalchand Kokal, 'Crude Oil Emulsions: A State-Of-The-Art Review' ; SPE journal, Vol.20, 2005.

Kokal, S.L. and Sayegh, S.G., “Asphaltenes: The Cholesterol of Petroleum”, SPE journal, March ( 1995).

J.E. Strassner, "Effect of pH on Interfacial Films and Stability of Crude Oil-Water Emulsions ", Journal of Petroleum Technology, Society of Petroleum Engineer,V.20,pp 308-309, March 1968.

Strassner, J.E., "Effect of pH on Interfacial Films and Stability of Crude Oil-Water Emulsions", J. Petrol. Technol, March (1968) , pp 303-312

Salager, J.L., "The Fundamental Basis for the Action of a Chemical Dehydrant: Influence of Physical and Chemical Formulation on the Stability of an Emulsion", Int. Chem. Eng., Vol 30No1, pages 103-116 (1990).

A.M.Alsabagha,M.E.Hassanb , S.E.M.Desoukya, N.M.Nassera , E.A.Elsharakya, M.M.Abdelhamid, " Demulsification of W/O emulsion at petroleum field and reservoir conditions using some demulsifiers based on polyethylene and propylene oxides" , Egyptian Journal of Petroleum, Volume 25,No.4, Pages 585-595, December 2016 .

J.G. Delgado-Linares, J.C. Pereira , M.Rondón, J. Bullón, J.-L. Salager , " Breaking of water-in-crude oil emulsions. Estimating the demulsifier performance at optimum formulation from both the required dose and the attained instability"; Energy Fuels, Vol.30 No6 ,pages 5483-5491,(2016).

J. Czarnecki, P. Tchoukov, T. Dabros ; "Possible role of asphaltenes in the stabilization of water-in-crude oil emulsions" ; Energy Fuels, Vol.26 (2012), pp. 5782-5786.

Paul M. Mcelfresh , David Lee Holcomb , Daniel Ector , "Application of nanofluid technology to improve recovery in oil and gas", Society of Petroleum Engineers, (June 2012).

M. Fortuny, C.B.Z. Oliveira, R.L.F.V. Melo, M. Nele, R.C.C. Coutinho, A.F. Santos, "Effect of salinity, temperature, water content, and pH on the microwave demulsification of crude oil emulsions" , Energy Fuels,Vol. 21 ,pages 1358-1364,(2007).

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Published

2021-03-30

How to Cite

Alkarbalaee, A. R., Hammadi, A. S., & Abdul Majeed, G. H. (2021). Treating Wet Oil in Amara Oil Field Using Nanomaterial (SiO2) With Different Types of De emulsifiers. Iraqi Journal of Chemical and Petroleum Engineering, 22(1), 29-38. https://doi.org/10.31699/IJCPE.2021.1.4

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