Abstract
In this study, free volume theory (FVT) in combination with perturbed-chain statistical associating fluid theory is implemented for viscosity prediction of petroleum reservoir fluids containing ill-defined components such as cuts and plus fractions. FVT has three adjustable parameters for each component to calculate viscosity. These three parameters for petroleum cuts (especially plus fractions) are not available. In this work, these parameters are determined for different petroleum fractions. A model as a function of molecular weight and specific gravity is developed using 22 real reservoir fluid samples with API grades in the range of 22 to 45. Afterward, the proposed model accuracy in comparison with the accuracy of De la Porte et al. with reference to experimental data is presented. The presented model is used for six real samples in an evaluation step, and the results are compared with available experimental data and the method of De la Porte et al. Finally, the method of Lohrenz et al. and the method of Pedersen et al. as two common industrial methods for viscosity calculation are compared with the proposed approach. The absolute average deviation was 9.7 % for free volume theory method, 15.4 % for Lohrenz et al., and 22.16 for Pedersen et al.
Similar content being viewed by others
Abbreviations
- A res :
-
Residual Helmholtz free energy
- \( \tilde{a}^{res} \) :
-
Reduced residual Helmholtz free energy
- \( \tilde{a}^{hc} \) :
-
Hard chain contribution to reduced Helmholtz free energy
- \( \tilde{a}^{disp} \) :
-
Dispersion contribution to reduced Helmholtz free energy
- \( AD\%_{FVT} = 100.\left| {\frac{{\upmu^{exp} -\upmu^{FVT} }}{{\upmu^{exp} }}} \right| \) :
-
Absolute deviation percent of calculated viscosity by FVT model
- \( AD\%_{LBC} = 100.\left| {\frac{{\upmu^{exp} -\upmu^{LBC} }}{{\upmu^{exp} }}} \right| \) :
-
Absolute deviation percent of calculated viscosity by LBC method
- B :
-
Characteristic of free volume overlap
- EOS :
-
Equation of state
- VS :
-
Volume shift
- E :
-
Necessary energy to form a free space available for a molecule to diffuse
- E 0 :
-
Barrier energy for molecule to diffuse
- \( F_{c} \) :
-
Correction factor
- fv :
-
Volume fraction
- K:
-
Boltzmann constant
- L :
-
Average characteristic molecular quadratic length
- MW :
-
Molecular weight
- \( M_{w} \) :
-
Molecular weight
- MW_plus fraction:
-
Molecular weight of plus fraction
- m :
-
Segment length
- N :
-
Avogadro number
- N A :
-
Avogadro number
- N t :
-
Total mole in the cell
- N L :
-
Liquid mole number in the cell
- N G :
-
Gas mole number in the cell
- \( OF\left( {a,b,c} \right) = \frac{1}{n}.\sum \left| {\frac{{\upmu^{exp} -\upmu^{calc} }}{{\upmu^{exp} }}} \right| \) :
-
Objective function for viscosity
- Pc :
-
Critical pressure
- Pbubble :
-
Bubble point pressure
- R:
-
Universal gas constant
- SP.GR:
-
Specific gravity
- S_plus fraction:
-
Specific gravity of plus fraction
- T:
-
Temperature (K)
- Tc :
-
Critical temperature
- Vc :
-
Critical volume
- V l :
-
Liquid volume
- V g :
-
Gas volume
- x:
-
Liquid composition
- xi :
-
Mole fraction of species i
- y :
-
Gas composition
- Zhc :
-
Hard chain contribution of compressibility factor
- Zdisp :
-
Dispersion contribution of compressibility factor
- Z g :
-
Gas compressibility factor
- Z l :
-
Liquid compressibility factor
- ε:
-
Depth of potential
- η:
-
Viscosity
- \( \upeta_{0} \) :
-
Dilute gas viscosity
- \( \Delta\upeta \) :
-
Dense state viscosity
- η:
-
Packing fraction density
References
A. Allal, M. Moha-Ouchane, C. Boned, Phys. Chem. Liq. 39, 1–30 (2001)
A. Allal, C. Boned, A. Baylaucq, Phys. Rev. E Stat. Nonlinear Soft Matter. Phys. 64, 101–110 (2001)
J.H. Dymond, M.A. Awan, Int. J. Thermophys. 10, 941–951 (1989)
M. Assael, J. Dymond, M. Papadaki, P. Patterson, Fluid Phase Equilib. 75, 245–255 (1992)
S.E. Quiñones-Cisneros, C.K. Zéberg-Mikkelsen, E.H. Stenby, Fluid Phase Equilib. 169, 249–276 (2000)
S.E. Quiñones-Cisneros, C.K. Zéberg-Mikkelsen, E.H. Stenby, Fluid Phase Equilib. 178, 1–16 (2001)
S.E. Quiñones-Cisneros, U.K. Deiters, J. Phys. Chem. B 110, 12820–12834 (2006)
T. Goel, C.N. Patra, T. Mukherjee, C. Chakravarty, J. Chem. Phys. 129, 164–174 (2008)
G. Galliero, C. Boned, J. Fernández, J. Chem. Phys. 134, 64–74 (2011)
L.T. Novak, Int. J. Chem. Reactor Eng. 9, 1–20 (2011)
A.S. de Wijn, V. Vesovic, G. Jackson, J.M. Trusler, J. Chem. Phys. 128, 204–214 (2008)
R. Srivastava, D.K. Dwivedee, K.N. Khanna, J. Mol. Liq. 139, 29–34 (2008)
G. Galliéro, C. Boned, A. Baylaucq, Ind. Eng. Chem. Res. 44, 6963–6972 (2005)
G. Galliero, C. Boned, Phys. Rev. E Stat. Phys. Plasmas Fluids 79, 102–120 (2009)
M.S. Zabaloy, J.M. Machado, E.A. Macedo, Int. J. Thermophys. 22, 829–858 (2001)
M.S. Zabaloy, V.R. Vasquez, E.A. Macedo, J. Supercrit. Fluids 36, 106–117 (2005)
A. Allal, C. Boned, P. Daugé, Phys. Chem. Liq. 39, 607–624 (2001)
A. Baylaucq, M. Comuñas, C. Boned, A. Allal, J. Fernández, Fluid Phase Equilib. 199, 249–263 (2002)
C.K. Zéberg-Mikkelsen, A. Baylaucq, M. Barrouhou, C. Boned, Phys. Chem. Chem. Phys. 5, 1547–1551 (2003)
M. Comuñas, A. Baylaucq, F. Plantier, C. Boned, J. Fernández, Fluid Phase Equilib. 222, 331–338 (2004)
P. Reghem, A. Baylaucq, M. Comunas, J. Fernández, C. Boned, Fluid Phase Equilib. 236, 229–236 (2005)
D.l. Porte, in Sensitivities to Component Characterizations of Heavy Oil Viscosity in Numerical Reservoir Simulation of Steam-Injection Processes (Chemical Engineering Department, Imperial College, London, 2012)
E. Behzadfar, S.G. Hatzikiriakos, Fuel 116, 578–587 (2014)
M. Almasi, J. Chem. Eng. Data 60, 714–720 (2015)
J.J. De la Porte, C.A. Kossack, Fuel 136, 156–164 (2014)
G. Soave, Chem. Eng. Sci. 27, 1197–1203 (1972)
D.-Y. Peng, D.B. Robinson, Ind. Eng. Chem. Fundam. 15, 59–64 (1976)
W.G. Chapman, K.E. Gubbins, G. Jackson, M. Radosz, Ind. Eng. Chem. Res. 29, 1709–1721 (1990)
W.G. Chapman, G. Jackson, K.E. Gubbins, Mol. Phys. 65, 1057–1079 (1988)
S.H. Huang, M. Radosz, Ind. Eng. Chem. Res. 29, 2284–2294 (1990)
S.H. Huang, M. Radosz, Ind. Eng. Chem. Res. 30, 1994–2005 (1991)
J. Gross, G. Sadowski, Ind. Eng. Chem. Res. 40, 1244–1260 (2001)
M. Assareh, C. Ghotbi, M. Tavakkoli, G. Bashiri, Fluid Phase Equilib. 408, 273–283 (2016)
F. Varzandeh, E.H. Stenby, W. Yan, Fluid Phase Equilib. 433, 97–111 (2017)
S.P. Tan, H. Adidharma, B.F. Towler, M. Radosz, Ind. Eng. Chem. Res. 44, 8409–8418 (2005)
S.P. Tan, H. Adidharma, B.F. Towler, M. Radosz, Ind. Eng. Chem. Res. 45, 2116–2122 (2006)
W.A. Burgess, D. Tapriyal, I.K. Gamwo, B.D. Morreale, M.A. McHugh, R.M. Enick, Ind. Eng. Chem. Res. 51, 16721–16733 (2012)
F. Llovell, R.M. Marcos, L.F. Vega, J. Phys. Chem. B 117, 8159–8171 (2013)
S.E. Quiñones-Cisneros, C.K. Zéberg-Mikkelsen, E.H. Stenby, Chem. Eng. Sci. 56, 7007–7015 (2001)
S.E. Quiñones-Cisneros, C.K. Zéberg-Mikkelsen, J. Fernández, J. García, AIChE J. 52, 1600–1610 (2006)
S. Quiñones-Cisneros, C. Zéberg-Mikkelsen, A. Baylaucq, C. Boned, Int. J. Thermophys. 25, 1353–1366 (2004)
K.A.G. Schmidt, S.E. Quiñones-Cisneros, B. Kvamme, Energy Fuels 19, 1303–1313 (2005)
R. Bagherinia, M. Assareh, F. Feyzi, Fluid Phase Equilib. 425, 21–30 (2016)
Y.H. Dehaghani, M. Assareh, F. Feyzi, Fluid Phase Equilib. 1, 14 (2017)
J. Lohrenz, B.G. Bray, C.R. Clark, J. Pet. Technol. 231, 1117–1127 (1964)
K.S. Pedersen, A. Fredenslund, P.L. Christensen, P. Thomassen, Chem. Eng. Sci. 39, 1011–1016 (1984)
M.R. Riazi, T.E. Daubert, Ind. Eng. Chem. Res. 26, 755–759 (1987)
B.I. Lee, M.G. Kesler, AIChE J. 21, 510–527 (1975)
C.H. Whitson, in Topics on Phase Behavior and Flow of Petroleum Reservoir Fluids (Norwegian Institute of Technology, Department of Petroleum and Chemical Engineering, University of Trondheim, 1983)
W. Yan, F. Varzandeh, E.H. Stenby, Fluid Phase Equilib. 386, 96–124 (2015)
X. Liang, W. Yan, K. Thomsen, G.M. Kontogeorgis, Fluid Phase Equilib. 375, 254–268 (2014)
X. Liang, W. Yan, K. Thomsen, G.M. Kontogeorgis, Fluid Phase Equilib. 406, 147–155 (2015)
I. Polishuk, Ind. Eng. Chem. Res. 53, 14127–14141 (2014)
T.H. Chung, L.L. Lee, K.E. Starling, Ind. Eng. Chem. Fundam. 23, 8–13 (1984)
T.H. Chung, M. Ajlan, L.L. Lee, K.E. Starling, Ind. Eng. Chem. Res. 27, 671–679 (1988)
C. Wilke, J. Chem. Phys. 18, 517–519 (1950)
L. Zipperer, F. Herning, Das Gas-und Wasserfach 4, 49–59 (1936)
C. Boned, C.K. Zéberg-Mikkelsen, A. Baylaucq, P. Daugé, Fluid Phase Equilib. 212, 143–164 (2003)
X. Canet, P. Dauge, A. Baylaucq, C. Boned, C.K. Zéberg-Mikkelsen, S.E. Quiñones-Cisneros, E.H. Stenby, Int. J. Thermophys. 22, 1669–1689 (2001)
A.M. Elsharkawy, S.A. Hassan, Y.S. Hashim, M.A. Fahim, Ind. Eng. Chem. Res. 42, 4132–4142 (2003)
M. Al-Ajmi, P.C. Tybjerg, C.P. Rasmussen, J.A. Shaikh, in SPE Middle East Oil and Gas Show and Conference (Society of Petroleum Engineers, 2011)
W.D. McCain, The Properties of Petroleum Fluids (PennWell Books, Houston, 1990)
K.S. Pedersen, P.L. Christensen, J.A. Shaikh, Phase Behavior of Petroleum Reservoir Fluids (CRC Press, Boca Raton, 2014)
K.S. Pedersen, A. Fredenslund, P. Thomassen, Properties of Oils and Natural Gases (Gulf Pub Co, Houston, 1989)
M.A. Barrufet, K.R. Hall, A. Estrada-Baltazar, G.A. Iglesias-Silva, J. Chem. Eng. Data 44, 1310–1314 (1999)
D. Ducoulombier, H. Zhou, C. Boned, J. Peyrelasse, H. Saint-Guirons, P. Xans, J. Phys. Chem. 90, 1692–1700 (1986)
G.A. Iglesias-Silva, A. Estrada-Baltazar, K.R. Hall, M.A. Barrufet, J. Chem. Eng. Data 44, 1304–1309 (1999)
A.J. Queimada, S. Quinones-Cisneros, I.M. Marrucho, J.A. Coutinho, E.H. Stenby, Int. J. Thermophys. 24, 1221–1239 (2003)
Author information
Authors and Affiliations
Corresponding author
Rights and permissions
About this article
Cite this article
Khoshnamvand, Y., Assareh, M. Viscosity Prediction for Petroleum Fluids Using Free Volume Theory and PC-SAFT. Int J Thermophys 39, 54 (2018). https://doi.org/10.1007/s10765-018-2377-0
Received:
Accepted:
Published:
DOI: https://doi.org/10.1007/s10765-018-2377-0