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The Model to Predict the Viscosity of Hydrocarbon Mixtures Containing CO2

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Proceedings of the International Field Exploration and Development Conference 2023 (IFEDC 2023)

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Abstract

The viscosity of hydrocarbon mixtures is essential for CO2 storage applications in depleted oil field. Furthermore, it is necessary to understand the impact of CO2 on characteristics of hydrocarbon mixtures in order to assess the extent to which viscous fingering, gravity segregation, hydrodynamic dispersion and interfacial tension affects influence the local displacement efficiency during miscible gas flooding processes. Whilst the phase behaviour of carbon dioxide/hydrocarbon binary mixtures has been widely reported, empirical data relating to relevant fluid densities and viscosities are frequently absent due to lack of measurements.

The extended hard-sphere model (EHS) and the 1-component Extended Hard-Sphere model (1-cEHS) have been modified and tested against experimental data to predict the viscosity of hydrocarbon mixtures containing CO2. The existing expression for the molar core volume and roughness factor for long chain n-alkanes were used. A new correlation for molar core volume V0 of pure CO2 was obtained by the regression of the experimental data. To ensure the validity of CO2 for use in the scheme for n-alkanes, CO2 was regarded as a pseudo n-alkane component which is characterized by an effective molecular weight.

For multi-component (CO2/n-C6, C7, C8, C12) and binary systems of CO2/n-alkanes, including n-hexane, n-decane, n-tetradecane, n-hexadecane, and n-octadecane, the mixtures of various CO2 fractions were compared with the results from the existing literature. In most of the available studies, it has not been difficult to identify that the simple mixing rule is usually not the best choice for predicting a mixture’s viscosity. However, the EHS model behaves better than the 1-cEHS model in the limit of low levels of CO2 content.

Copyright 2023, IFEDC Organizing Committee.

This paper was prepared for presentation at the 2023 International Field Exploration and Development Conference in Urumqi, China, 16–18 August, 2023.

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References

  1. Barrufet, M., Salem, S., Tantawy, M., Iglesias-Silva, G.: Liquid viscosities of carbon dioxide + hydrocarbons from 310 K to 403 K. J. Chem. Eng. Data 41(3), 436–439 (1996). https://doi.org/10.1021/je950256y

    Article  Google Scholar 

  2. Turek, E., Metcalfs, R., Yarborough, L., Robinson, R.: Phase equilibria in CO2-multicomponent hydrocarbon systems: experimental data and an improved prediction technique. Soc. Petrol. Eng. J. 24(03), 308–324 (1984). https://doi.org/10.2118/9231-pa

    Article  Google Scholar 

  3. Cullick, A., Mathis, M.: Densities and viscosities of mixtures of carbon dioxide and n-decane from 310 to 403 K and 7 to 30 MPa. J. Chem. Eng. Data 29(4), 393–396 (1984). https://doi.org/10.1021/je00038a008

    Article  Google Scholar 

  4. Ciotta, F., Trusler, J., Vesovic, V.: Extended hard-sphere model for the viscosity of dense fluids. Fluid Phase Equilib. 363, 239–247 (2014). https://doi.org/10.1016/j.fluid.2013.11.032

    Article  Google Scholar 

  5. Nguyen, T., Riesco, N., Vesovic, V.: Predicting the viscosity of n -alkane liquid mixtures based on molecular description. Fuel 208, 363–376 (2017). https://doi.org/10.1016/j.fuel.2017.07.015

    Article  Google Scholar 

  6. Kian, K., Scurto, A.: Viscosity of compressed CO2-saturated n -alkanes: CO2/n-hexane, CO2/n-decane, and CO2/n-tetradecane. J. Supercrit. Fluids 133, 411–420 (2018). https://doi.org/10.1016/j.supflu.2017.10.030

    Article  Google Scholar 

  7. Nourozieh, H., Kariznovi, M., Abedi, J.: Measurement and correlation of saturated liquid properties and gas solubility for decane, tetradecane and their binary mixtures saturated with carbon dioxide. Fluid Phase Equil. 337, 246–254 (2013)

    Article  Google Scholar 

  8. Kariznovi, M., Nourozieh, H., Abedi, J.: Phase composition and saturated liquid properties in binary and ternary systems containing carbon dioxide, n-decane, and n-tetradecane. J. Chem. Thermodyn. 57, 189–196 (2013)

    Article  Google Scholar 

  9. Mohammed, M., Ciotta, F., Trusler, J.: Viscosities and densities of binary mixtures of hexadecane with dissolved methane or carbon dioxide at temperatures from (298 to 473) K and at pressures up to 120 MPa. J. Chem. Eng. Data 62(1), 422–439 (2016). https://doi.org/10.1021/acs.jced.6b00750

    Article  Google Scholar 

  10. Nourozieh, H., Bayestehparvin, B., Kariznovi, M., Abedi, J.: Equilibrium properties of (carbon dioxide + n-decane + n-octadecane) systems: experiments and thermodynamic modeling. J. Chem. Eng. Data 58, 1236–1243 (2013)

    Article  Google Scholar 

  11. Kariznovi, M., Nourozieh, H., Abedi, J.: Experimental results and thermodynamic investigation of carbon dioxide solubility in heavy liquid hydrocarbons and corresponding phase properties. Fluid Phase Equilib. 339, 105–111 (2013)

    Article  Google Scholar 

  12. Ciotta, F.: Viscosity of Asymmetric Liquid Mixtures under Extreme Conditions. Imperial College London, Ph.D. Thesis (2010)

    Google Scholar 

  13. Assael, M.J., Dymond, J.H., Papadaki, M., Patterson, P.M.: Correlation and prediction of dense fluid transport-coefficients. I. Normal-alkanes. Int. J. Thermophys. 13, 269–281 (1992)

    Article  Google Scholar 

  14. Riesco, N., Vesovic, V.: Extended hard-sphere model for predicting the viscosity of long-chain n-alkanes. Fluid Phase Equilib. 425, 385–392 (2016)

    Article  Google Scholar 

  15. Vesovic, V., Wakeham, W.A.: Prediction of the viscosity of fluid mixtures over wide ranges of temperature and pressure. Chem. Eng. Sci. 44, 2181–2189 (1989)

    Article  Google Scholar 

  16. Ciotta, F., Maitland, G., Smietana, M., Trusler, J.P.M., Vesovic, V.: Viscosity and density of carbon dioxide + 2,6,10,15,19,23-hexamethyltetracosane (squalane). J. Chem. Eng. Data 54, 2436–2443 (2009)

    Article  Google Scholar 

  17. Vesovic, V., Wakeham, W.A., Olchowy, G.A., Sengers, J.V., Watson, J.T.R., Millat, J.: The transport-properties of carbon-dioxide. J. Phys. Chem. Ref. Data. Ref. Data 19, 763–808 (1990)

    Article  Google Scholar 

  18. Lemmon, E.W., Huber, M.L., McLinden, M.O.: NIST Standard Reference Database 23: Reference Fluid Thermodynamic and Transport Properties-REFPROP, Version 9.1. National Institute of Standards and Technology (2013)

    Google Scholar 

  19. Fenghour, A., Wakeham, W., Vesovic, V.: The viscosity of carbon dioxide. J. Phys. Chem. Ref. Data 27(1), 31–44 (1998). https://doi.org/10.1063/1.556013

    Article  Google Scholar 

  20. Assael, M.J., Dymond, J.H., Papadaki, M., Patterson, P.M.: Correlation and prediction of dense fluid transport coefficients. III. Normal-alkane Mixtures. Int. J. Thermophys. 13, 659–669 (1992)

    Google Scholar 

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Acknowledgments

The project is supported by China National Petroleum Corporation, 《Study on new technology of EOR in complex fault block and buried hill Oilfield 》(Number: 2021DJ1105). And Science and Technology Project of PetroChina Exploration and Production Company《Pilot test of carbon flooding and carbon storage in buried hills in North China》(Number: 2022ZS0807).

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Yan, X., Wang, Rs., Zeng, Qq., Guo, Fj. (2024). The Model to Predict the Viscosity of Hydrocarbon Mixtures Containing CO2. In: Lin, J. (eds) Proceedings of the International Field Exploration and Development Conference 2023. IFEDC 2023. Springer Series in Geomechanics and Geoengineering. Springer, Singapore. https://doi.org/10.1007/978-981-97-0268-8_38

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  • DOI: https://doi.org/10.1007/978-981-97-0268-8_38

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