Assessment of Non-Equilibrium Phase Behavior Model Parameters for Oil and Gas-Condensate Systems by Laboratory and Field Studies (Russian)

2020 ◽  
Author(s):  
Ilya Mikhailovich Indrupskiy ◽  
Mikhail Yurievich Danko ◽  
Timur Nikolaevich Tsagan-Mandzhiev ◽  
Ayguzel Ilshatovna Aglyamova
2020 ◽  
Author(s):  
Ilya Mikhailovich Indrupskiy ◽  
Mikhail Yurievich Danko ◽  
Timur Nikolaevich Tsagan-Mandzhiev ◽  
Ayguzel Ilshatovna Aglyamova

Author(s):  
Ilya M. Indrupskiy ◽  
Olga A. Lobanova ◽  
Vadim R. Zubov

Numerical models widely used for hydrocarbon phase behavior and compositional flow simulations are based on assumption of thermodynamic equilibrium. However, it is not uncommon for oil and gas-condensate reservoirs to exhibit essentially non-equilibrium phase behavior, e.g., in the processes of secondary recovery after pressure depletion below saturation pressure, or during gas injection, or for condensate evaporation at low pressures. In many cases the ability to match field data with equilibrium model depends on simulation scale. The only method to account for non-equilibrium phase behavior adopted by the majority of flow simulators is the option of limited rate of gas dissolution (condensate evaporation) in black oil models. For compositional simulations no practical yet thermodynamically consistent method has been presented so far except for some upscaling techniques in gas injection problems. Previously reported academic non-equilibrium formulations have a common drawback of doubling the number of flow equations and unknowns compared to the equilibrium formulation. In the paper a unified thermodynamically-consistent formulation for compositional flow simulations with non-equilibrium phase behavior model is presented. Same formulation and a special scale-up technique can be used for upscaling of an equilibrium or non-equilibrium model to a coarse-scale non-equilibrium model. A number of test cases for real oil and gas-condensate mixtures are given. Model implementation specifics in a flow simulator are discussed and illustrated with test simulations. A non-equilibrium constant volume depletion algorithm is presented to simulate condensate recovery at low pressures in gas-condensate reservoirs. Results of satisfactory model matching to field data are reported and discussed.


2019 ◽  
Author(s):  
Faisal Al-Jenaibi ◽  
Kirill Bogachev ◽  
Sergey Milyutin ◽  
Sergey Zemtsov ◽  
Evgenii Gusarov ◽  
...  

2020 ◽  
Vol 506 ◽  
pp. 112410
Author(s):  
Yang Yang ◽  
Zengmin Lun ◽  
Rui Wang ◽  
Wei Hu

2021 ◽  
Vol 2090 (1) ◽  
pp. 012138
Author(s):  
I M Indrupskiy ◽  
P A Chageeva

Abstract Mathematical models of phase behavior are widely used to describe multiphase oil and gas-condensate systems during hydrocarbon recovery from natural petroleum reservoirs. Previously a non-equilibrium phase behavior model was proposed as an extension over generally adopted equilibrium models. It is based on relaxation of component chemical potentials difference between phases and provides accurate calculations in some typical situations when non-instantaneous changing of phase fractions and compositions in response to variations of pressure or total composition is to be considered. In this paper we present a thermodynamic analysis of the relaxation model. General equations of non-equilibrium thermodynamics for multiphase flows in porous media are considered, and reduced entropy balance equation for the relaxation process is obtained. Isotropic relaxation process is simulated for a real multicomponent hydrocarbon system with different values of characteristic relaxation time using the non-equilibrium model implemented in the PVT Designer module of the RFD tNavigator simulation software. The results are processed with a special algorithm implemented in Matlab to calculate graphs of the total entropy time derivative and its constituents in the entropy balance equation. It is shown that the constituents have different signs, and the greatest influence on the entropy is associated with the interphase flow of the major component of the mixture and the change of the total system volume in the isotropic process. The characteristic relaxation time affects the rate at which the entropy is approaching its maximum value.


Fuel ◽  
2020 ◽  
Vol 272 ◽  
pp. 117648 ◽  
Author(s):  
Hongyang Wang ◽  
Farshid Torabi ◽  
Fanhua Zeng ◽  
Huiwen Xiao

2019 ◽  
Vol 52 (15) ◽  
pp. 5811-5818
Author(s):  
Deul Kim ◽  
Moon Ryul Sihn ◽  
Min-Gi Jeon ◽  
Guangcui Yuan ◽  
Sushil K. Satija ◽  
...  

2017 ◽  
Vol 254 (12) ◽  
pp. 1600862 ◽  
Author(s):  
Szymon Maćkowiak ◽  
David M. Heyes ◽  
Slawomir Pieprzyk ◽  
Daniele Dini ◽  
Arkadiusz C. Brańka

Sign in / Sign up

Export Citation Format

Share Document