Developing a K-value equation for predict dew point pressure of gas condensate reservoirs at high pressure

Seyedfoad Aghamiri , Mohsen Tamtaji , Mohammad Javad Ghafoori

Petroleum ›› 2018, Vol. 4 ›› Issue (4) : 437 -443.

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Petroleum ›› 2018, Vol. 4 ›› Issue (4) :437 -443. DOI: 10.1016/j.petlm.2017.08.002
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Developing a K-value equation for predict dew point pressure of gas condensate reservoirs at high pressure
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Abstract

This paper proposed a new empirical K-value equation is developed to calculate dew pressure for gas condensate reservoirs. This equation is applicable in the wide ranges of composition, temperature, and pressure by considering the effect of composition via two equations for normal boiling point and critical temperature of the mixture. The range of dew pressure, temperature, heptane plus mole fraction, methane mole fraction, N2 mole fraction, CO2 mole fraction, and H2S mole fraction are fallen into 2666.7-9655 Psia, 40-350.87 °F, 0.0021-0.213, 0.3344-0.9668, 0-0.4322, 0-0.0864, and 0-0.942 respectively. As an important point, the proposed equation has any adjustable parameters, in addition, this equation indicates that in order to predict of dew pressure of gas condensate reservoirs, trial and error was not needed and therefore, computational speed increases beyond the accuracy. Moreover, the accuracy is validated by comparing against the experimental data of 81 gas condensate reservoirs samples from published literature and the results of Wilson, Whitson, and Ghafoori equations. Compared to the experimental data, the absolute average deviations of dew pressure calculations for the proposed equation, Wilson, Whitson, and Ghafoori were 7.6%, 97.6%, 99.4%, and 94.9% respectively.

Keywords

Dew point pressure / Gas condensate reservoirs / K-value / Wilson

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Seyedfoad Aghamiri, Mohsen Tamtaji, Mohammad Javad Ghafoori. Developing a K-value equation for predict dew point pressure of gas condensate reservoirs at high pressure. Petroleum, 2018, 4(4): 437-443 DOI:10.1016/j.petlm.2017.08.002

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References

[1]

V. Louli, G. Pappa, C. Boukouvalas, S. Skouras, E. Solbraa, K.O. Christensen, E. Voutsas, Measurement and prediction of dew point curves of natural gas mixtures, Fluid Phase Equilibria 334 (2012) 1-9.

[2]

M.J. Ghafoori, S.F. Aghamiri, M.R. Talaie, A new empirical K-value equation for reservoir fluids, Fuel 98 (2012) 236-242.

[3]

S. Nowroozi, M. Ranjbar, H. Hashemipour, M. Schaffie, Development of a neural fuzzy system for advanced prediction of dew point pressure in gas condensate reservoirs, Fuel Process. Technol. 90 (2009) 452-457.

[4]

M.A. Ahmadi, A. Elsharkawy, Robust correlation to predict dew point pressure of gas condensate reservoirs, Petroleum (2016) 1-8.

[5]

A.M. Elsharkawy, Predicting the dew point pressure for gas condensate reservoirs: empirical models and equations of state, Fluid Phase Equilibria 193 (2002) 147-165.

[6]

M.R. Maleki, F. Rashidi, H. Mahani, E. Khamehchi, A simulation study of the enhancement of condensate recovery from one of the Iranian naturally fractured condensate reservoirs, J. Pet. Sci. Eng. 92 (2012) 158-166.

[7]

L. Yong, Z. Jing, W. Xueyong, J. Yuwei, Y. Jie, A new reservoir simulation approach for fractured gas-condensate reservoirs, Pet. Explor. Dev. 37 (2010) 592-595.

[8]

J. Mazloom, F. Rashidi, R. Kelly, A novel approach to the calculation of the distance of a sealing fault from a well in a gas condensate reservoir, J. Pet. Sci. Eng. 45 (2004) 149-158.

[9]

L. Vega, M. Barrufet, Analysis of a non-volumetric gas-condensate reservoir using a generalized material balance equation with fluid properties from an equation of state, J. Pet. Sci. Eng. 48 (2005) 105-119.

[10]

R.A. Almehaideb, I. Ashour, K.A. El-Fattah, Improved K-value correlation for UAE crude oil components at high pressures using PVT laboratory data, Fuel 82 (2003) 1057-1065.

[11]

R. Almehaideb, M. Abdulkarim, A. Al-Khanbashi, Improved K-values correlation for UAE crude oil components at low pressures using PVT laboratory data, Fuel 80 (2001) 117-124.

[12]

M. Standing, A set of equations for computing equilibrium ratios of a crude oil/natural gas system at pressures below 1000 psia, J. Pet. Technol. 31 (1979) 1193-1195.

[13]

T. Ahmed, Equations of State and PVT Analysis, 2007.

[14]

A. Hoffman, J. Crump, C. Hocott, Equilibrium constants for a gascondensate system, J. Pet. Technol. 5 (1953) 1-10.

[15]

T. Ahmed, Reservoir Engineering Handbook, Access Online via Elsevier, 2005.

[16]

C. Whitson, S. Torp,Evaluating constant volume depletion data, in:SPE Annual Technical Conference and Exhibition, 1981.

[17]

M.L. McWilliams, An equation to relate K-factors to pressure and temperature, Chem. Eng. 80 (1973) 138-140.

[18]

M.R. Riazi, Characterization and Properties of Petroleum Fractions, 2005.

[19]

J.M. Smith, H.C.V. Ness, M.M. Abbott, Introduction to Chemical Engineering Thermodynamics, seventh ed., 2005.

[20]

A. Danesh, PVT and Phase Behaviour of Petroleum Reservoir Fluids, vol. 47, Elsevier, 1998.

[21]

C.H. Whitson, M.R. Brulé, Phase Behavior, Henry L. Doherty Memorial Fund of AIME, Society of Petroleum Engineers, Richardson, Tex, 2000.

[22]

M.J. Rzasa, E.D. Glass, J.B. Opfell, Prediction of critical properties and equilibrium vaporization constants for complex hydrocarbon systems, in: Chemical Engineering Progress Symposium Series, vol. 48, American Institute of Chemical Engineers, 345 E 47th St, New York, NY 10017, 1952 Jan, pp. 28-37. No. 2.

[23]

S.M.J. Majidi, A. Shokrollahi, M. Arabloo, R. Mahdikhani-Soleymanloo, M. Masihi, Evolving an accurate model based on machine learning approach for prediction of dew-point pressure in gas condensate reservoirs, Chem. Eng. Res. Des. 92 (5) (May 2014)891-902.

[24]

L.K. Nemeth. A Correlation of Dew-point Pressure with Reservoir Fluid Composition and Temperature, 1966.

[25]

T. Yang, W.D. Chen, T.M. Guo, Phase behavior of a near-critical reservoir fluid mixture, Fluid Phase Equilib 128 (1997) 183-197.

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