Effect of Fluid Viscosity on Asphalthene Deposition Rate during Turbulent Flow in Oil Wells

Gholamreza Vakili-Nezhaad; Nabeel Al-Rawahi; G. Ali Mansoori; Amin Fatemi

doi:doi:10.11648/j.ajche.20130102.13

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Effect of Fluid Viscosity on Asphalthene Deposition Rate during Turbulent Flow in Oil Wells

Gholamreza Vakili-Nezhaad, Nabeel Al-Rawahi, G. Ali Mansoori, Amin Fatemi

Published in American Journal of Chemical Engineering (Volume 1, Issue 2)

Received: 26 June 2013 Accepted: Published: 10 July 2013

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Abstract

The production and transportation of petroleum fluids will be severely affected by the deposition of suspended particles (i.e. asphaltenes, diamondoids, paraffin/wax, sand, etc.) in petroleum fluid production wells and/or transfer pipelines. Viscosity variations of petroleum fluid are an important phenomenon that could have significant effect on different properties related to petroleum fluid. Therefore, it is important to understand the effect of viscosity variations of petroleum fluid onthe deposition rate of suspended particles on the walls of the flowing channel. In this study, the analytical model for the prefouling behavior of suspended particles in production lines ischallenged in terms of viscosity changes that occur during the production in oil wells/tubings fora typical fluid sample experiencing particle deposition. Calculations of particle deposition rate inoil wells/tubings considering the change in viscosity for this typical oil sample is taken into consideration. The analysis presented in this report shows that rates of particle deposition (during petroleum fluid production) on the walls of the oil well/tubing is slightly effected by the viscosity variations that occur during the production conditions and it is also shown that the assumption of constant viscosity while deriving the analytical model for the deposition rate of particles on the walls of fluid conduits is quite a reasonable and valid assumption.

Published in	American Journal of Chemical Engineering (Volume 1, Issue 2)
DOI	10.11648/j.ajche.20130102.13
Page(s)	45-49
Creative Commons	This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited.
Copyright	Copyright © The Author(s), 2024. Published by Science Publishing Group

Keywords

Asphalthene, Deposition, Turbulent Flow, Viscosity, Oil Wells

References

[1]	Escobedo J. and G.A. Mansoori, "Prefouling Behavior of Suspended Particles in Petroleum Fluid Flow", SCINTIA IRANICA, Vol. 17, No. 1, 77-85 (2010).
[2]	Escobedo, J. and Mansoori, G.A. "Asphaltene and other heavy-organic particle deposition during transfer and production operations", SPE paper #30672, Proceed. Soc. of Petrol Eng. Annual. Tech. Conf. Held in Dallas, TX (22-25 Oct. 1995).
[3]	Vafaie-Sefti, M. Mousavi-Dehghani, S.A., Riazi, M.R., and Mansoori, G.A. "An analysis of methods for determination of onsets of asphaltene phase separations", J. Petrol Sci. & Eng., 42(2-4), pp. 145-156 (2004).
[4]	José L. Mendoza de la Cruz, Francisco J. Argüelles-Vivas, Víctor Matías-Pérez, Cecilia de los A. Durán-Valencia and Simón López-Ramírez,"Asphaltene-Induced Precipitation and Deposition During Pressure Depletion on a Porous Medium: An Experimental Investigation and Modeling Approach", Energy & Fuels 23 (2009), 5611–5625.
[5]	Friedlander, S.K. and Johnstone, H.F. "Deposition of suspended particles from turbulent gas streams", Ind. Eng. Chem., 49 (7), pp. 1151-1156, 1957.
[6]	M. Jamialahmadi, B. Soltani, H. Müller-Steinhagen, D. Rashtchian, "Measurement and prediction of the rate of deposition of flocculated asphaltene particles from oil", International Journal of Heat and Mass Transfer Volume 52, Issues 19–20, September 2009,4624-4634.
[7]	Beal, S.K. "Deposition of particles in turbulent flow on channel or pipe walls", Nuclear Sci. Eng., 40, pp. 1-11 (1970).
[8]	Lauufer, J. "The Structure of turbulence in fully developed pipe flow", NACA 1174, National Advisory Committee for Aeronautics (Available from NASA as TR-1174) (1954).
[9]	J. Escobedo, G.A. Mansoori, C. Balderas-Joers, L.J. Carranza-Becerra, M.A. Mendez-Garcia, Heavy Organic Deposition During Oil Production from a Hot Deep Reservoir: A Field Experience, SPE Paper #38989 (9), Proceedings of the 5th Latin American and Caribbean Petroleum Engineering Conference and Exhibition, Rio de Janeiro, Brazil, 30 August–3 September 1997.
[10]	Colebrook, C.F., 1939. Turbulent flow in pipes with particular reference to the transition region between the smooth and rough pipes laws. J. Inst. Civil Eng. 11, 133–156.
[11]	Dos Santos, J.S.T., Fernandes, A.C., Giulietti, M., 2004. Study of the paraffin deposit formation using the cold finger methodology for Brazilian crude oils. J. Pet. Sci. Eng. 45 (1–2), 47–60 (30 November).
[12]	Zougari M., Hammami A., Broze G. and Fuex N. Live oils novel organic solid deposition and control device: wax deposition validation, SPE Special Edition, 99538, 2005.
[13]	Zougari, M., Jacobs, S., Hammami, A., Broze, G., Flannery, M., Ratulowski, J., Stankiewicz, A., Novel organic solid deposition and control device for live oils: design and applications. Energy & Fuels 20 (2006), 1656–1663.
[14]	Zougari, M. Shear driven crude oil wax deposition evaluation, Journal of Petroleum Science and Engineering 70 (2010) 28–34.

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APA Style

Gholamreza Vakili-Nezhaad, Nabeel Al-Rawahi, G. Ali Mansoori, Amin Fatemi. (2013). Effect of Fluid Viscosity on Asphalthene Deposition Rate during Turbulent Flow in Oil Wells. American Journal of Chemical Engineering, 1(2), 45-49. https://doi.org/10.11648/j.ajche.20130102.13

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ACS Style

Gholamreza Vakili-Nezhaad; Nabeel Al-Rawahi; G. Ali Mansoori; Amin Fatemi. Effect of Fluid Viscosity on Asphalthene Deposition Rate during Turbulent Flow in Oil Wells. Am. J. Chem. Eng. 2013, 1(2), 45-49. doi: 10.11648/j.ajche.20130102.13

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AMA Style

Gholamreza Vakili-Nezhaad, Nabeel Al-Rawahi, G. Ali Mansoori, Amin Fatemi. Effect of Fluid Viscosity on Asphalthene Deposition Rate during Turbulent Flow in Oil Wells. Am J Chem Eng. 2013;1(2):45-49. doi: 10.11648/j.ajche.20130102.13

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@article{10.11648/j.ajche.20130102.13,
  author = {Gholamreza Vakili-Nezhaad and Nabeel Al-Rawahi and G. Ali Mansoori and Amin Fatemi},
  title = {Effect of Fluid Viscosity on Asphalthene Deposition Rate during Turbulent Flow in Oil Wells},
  journal = {American Journal of Chemical Engineering},
  volume = {1},
  number = {2},
  pages = {45-49},
  doi = {10.11648/j.ajche.20130102.13},
  url = {https://doi.org/10.11648/j.ajche.20130102.13},
  eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ajche.20130102.13},
  abstract = {The production and transportation of petroleum fluids will be severely affected by the deposition of suspended particles (i.e. asphaltenes, diamondoids, paraffin/wax, sand, etc.) in petroleum fluid production wells and/or transfer pipelines. Viscosity variations of petroleum fluid are an important phenomenon that could have significant effect on different properties related to petroleum fluid. Therefore, it is important to understand the effect of viscosity variations of petroleum fluid onthe deposition rate of suspended particles on the walls of the flowing channel. In this study, the analytical model for the prefouling behavior of suspended particles in production lines ischallenged in terms of viscosity changes that occur during the production in oil wells/tubings fora typical fluid sample experiencing particle deposition. Calculations of particle deposition rate inoil wells/tubings considering the change in viscosity for this typical oil sample is taken into consideration. The analysis presented in this report shows that rates of particle deposition (during petroleum fluid production) on the walls of the oil well/tubing is slightly effected by the viscosity variations that occur during the production conditions and it is also shown that the assumption of constant viscosity while deriving the analytical model for the deposition rate of particles on the walls of fluid conduits is quite a reasonable and valid assumption.},
 year = {2013}
}

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TY  - JOUR
T1  - Effect of Fluid Viscosity on Asphalthene Deposition Rate during Turbulent Flow in Oil Wells
AU  - Gholamreza Vakili-Nezhaad
AU  - Nabeel Al-Rawahi
AU  - G. Ali Mansoori
AU  - Amin Fatemi
Y1  - 2013/07/10
PY  - 2013
N1  - https://doi.org/10.11648/j.ajche.20130102.13
DO  - 10.11648/j.ajche.20130102.13
T2  - American Journal of Chemical Engineering
JF  - American Journal of Chemical Engineering
JO  - American Journal of Chemical Engineering
SP  - 45
EP  - 49
PB  - Science Publishing Group
SN  - 2330-8613
UR  - https://doi.org/10.11648/j.ajche.20130102.13
AB  - The production and transportation of petroleum fluids will be severely affected by the deposition of suspended particles (i.e. asphaltenes, diamondoids, paraffin/wax, sand, etc.) in petroleum fluid production wells and/or transfer pipelines. Viscosity variations of petroleum fluid are an important phenomenon that could have significant effect on different properties related to petroleum fluid. Therefore, it is important to understand the effect of viscosity variations of petroleum fluid onthe deposition rate of suspended particles on the walls of the flowing channel. In this study, the analytical model for the prefouling behavior of suspended particles in production lines ischallenged in terms of viscosity changes that occur during the production in oil wells/tubings fora typical fluid sample experiencing particle deposition. Calculations of particle deposition rate inoil wells/tubings considering the change in viscosity for this typical oil sample is taken into consideration. The analysis presented in this report shows that rates of particle deposition (during petroleum fluid production) on the walls of the oil well/tubing is slightly effected by the viscosity variations that occur during the production conditions and it is also shown that the assumption of constant viscosity while deriving the analytical model for the deposition rate of particles on the walls of fluid conduits is quite a reasonable and valid assumption.
VL  - 1
IS  - 2
ER  -

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Author Information

Gholamreza Vakili-Nezhaad

Department of Petroleum & Chemical Engineering, College of Engineering, Sultan Qaboos University, Muscat, Oman
Nabeel Al-Rawahi

Department of Mechanical & Industrial Engineering, College of Engineering, Sultan Qaboos University, Muscat, Oman
G. Ali Mansoori

Depts of Bioengineering, Chemical Engineering and Physics, University of Illinois at Chicago, Chicago, IL, USA
Amin Fatemi

Department of Geotechnology, Faculty of Civil Engineering and Geosciences, Delft University of Technology, Delft, Netherlands

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Plain Text BibTeX RIS

APA Style

Gholamreza Vakili-Nezhaad, Nabeel Al-Rawahi, G. Ali Mansoori, Amin Fatemi. (2013). Effect of Fluid Viscosity on Asphalthene Deposition Rate during Turbulent Flow in Oil Wells. American Journal of Chemical Engineering, 1(2), 45-49. https://doi.org/10.11648/j.ajche.20130102.13

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ACS Style

Gholamreza Vakili-Nezhaad; Nabeel Al-Rawahi; G. Ali Mansoori; Amin Fatemi. Effect of Fluid Viscosity on Asphalthene Deposition Rate during Turbulent Flow in Oil Wells. Am. J. Chem. Eng. 2013, 1(2), 45-49. doi: 10.11648/j.ajche.20130102.13

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AMA Style

Gholamreza Vakili-Nezhaad, Nabeel Al-Rawahi, G. Ali Mansoori, Amin Fatemi. Effect of Fluid Viscosity on Asphalthene Deposition Rate during Turbulent Flow in Oil Wells. Am J Chem Eng. 2013;1(2):45-49. doi: 10.11648/j.ajche.20130102.13

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@article{10.11648/j.ajche.20130102.13,
  author = {Gholamreza Vakili-Nezhaad and Nabeel Al-Rawahi and G. Ali Mansoori and Amin Fatemi},
  title = {Effect of Fluid Viscosity on Asphalthene Deposition Rate during Turbulent Flow in Oil Wells},
  journal = {American Journal of Chemical Engineering},
  volume = {1},
  number = {2},
  pages = {45-49},
  doi = {10.11648/j.ajche.20130102.13},
  url = {https://doi.org/10.11648/j.ajche.20130102.13},
  eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ajche.20130102.13},
  abstract = {The production and transportation of petroleum fluids will be severely affected by the deposition of suspended particles (i.e. asphaltenes, diamondoids, paraffin/wax, sand, etc.) in petroleum fluid production wells and/or transfer pipelines. Viscosity variations of petroleum fluid are an important phenomenon that could have significant effect on different properties related to petroleum fluid. Therefore, it is important to understand the effect of viscosity variations of petroleum fluid onthe deposition rate of suspended particles on the walls of the flowing channel. In this study, the analytical model for the prefouling behavior of suspended particles in production lines ischallenged in terms of viscosity changes that occur during the production in oil wells/tubings fora typical fluid sample experiencing particle deposition. Calculations of particle deposition rate inoil wells/tubings considering the change in viscosity for this typical oil sample is taken into consideration. The analysis presented in this report shows that rates of particle deposition (during petroleum fluid production) on the walls of the oil well/tubing is slightly effected by the viscosity variations that occur during the production conditions and it is also shown that the assumption of constant viscosity while deriving the analytical model for the deposition rate of particles on the walls of fluid conduits is quite a reasonable and valid assumption.},
 year = {2013}
}

Copy | Download

TY  - JOUR
T1  - Effect of Fluid Viscosity on Asphalthene Deposition Rate during Turbulent Flow in Oil Wells
AU  - Gholamreza Vakili-Nezhaad
AU  - Nabeel Al-Rawahi
AU  - G. Ali Mansoori
AU  - Amin Fatemi
Y1  - 2013/07/10
PY  - 2013
N1  - https://doi.org/10.11648/j.ajche.20130102.13
DO  - 10.11648/j.ajche.20130102.13
T2  - American Journal of Chemical Engineering
JF  - American Journal of Chemical Engineering
JO  - American Journal of Chemical Engineering
SP  - 45
EP  - 49
PB  - Science Publishing Group
SN  - 2330-8613
UR  - https://doi.org/10.11648/j.ajche.20130102.13
AB  - The production and transportation of petroleum fluids will be severely affected by the deposition of suspended particles (i.e. asphaltenes, diamondoids, paraffin/wax, sand, etc.) in petroleum fluid production wells and/or transfer pipelines. Viscosity variations of petroleum fluid are an important phenomenon that could have significant effect on different properties related to petroleum fluid. Therefore, it is important to understand the effect of viscosity variations of petroleum fluid onthe deposition rate of suspended particles on the walls of the flowing channel. In this study, the analytical model for the prefouling behavior of suspended particles in production lines ischallenged in terms of viscosity changes that occur during the production in oil wells/tubings fora typical fluid sample experiencing particle deposition. Calculations of particle deposition rate inoil wells/tubings considering the change in viscosity for this typical oil sample is taken into consideration. The analysis presented in this report shows that rates of particle deposition (during petroleum fluid production) on the walls of the oil well/tubing is slightly effected by the viscosity variations that occur during the production conditions and it is also shown that the assumption of constant viscosity while deriving the analytical model for the deposition rate of particles on the walls of fluid conduits is quite a reasonable and valid assumption.
VL  - 1
IS  - 2
ER  -

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