Analysis of near-miscible CO2-WAG displacements

The distinction between compositional and interfacial tension effects

Gang Wang, Gillian Pickup, Kenneth Sorbie, Eric Mackay, Arne Skauge

Research output: Chapter in Book/Report/Conference proceedingConference contribution

Abstract

CO2 Water-Alternating-Gas injection (CO2 WAG), which involves complex phase and flow behaviour, is still a challenging task to simulate and predict accurately. In this paper, we focus specifically on the regime of viscous fingering flow in CO2 WAG in heterogeneous systems because of its importance. We investigated two key physical processes that occur during near-Miscible WAG (nMWAG) processes, namely oil stripping (Mechanism 1, M1) and low-interfacial-tension (IFT) film flow effects (Mechanism 2, M2). The low IFT effects in M2 manifest themselves in an increased mobility of oil phase due to film flow process (discussed below). The importance of properly simulating the interaction of viscous, compositional (M1), and low-interfacial-tension effects (M2) is clearly demonstrated in this study. Our specific aim is to improve the modelling of CO2 displacement in the transition from immiscible to miscible flows in CO2 WAG processes. We simulated both immiscible and near-miscible CO2 WAG and also continuous CO2 displacements with unfavourable mobility ratios for 1D and 2D systems. 2D heterogeneous permeability fields were generated with certain Dykstra-Parsons coefficients and dimensionless correlation ranges. IFT (σgo) was calculated by the simulator as part of the compositional simulation using the McLeod-Sugden equation. The consequent IFT effects on relative permeability was imposed using two commonly used models, i.e. Coats (1980) and Betté et al. methods (1991), which have been implemented in many commercial software packages, such as CMG/GEM and E300. Thus, we identify two clear mechanisms of oil recovery that may occur in nearmiscible CO2 (or other gas) injection which we denote as, M1 for oil stripping or compositional effects, and M2 for low-IFT effects which are described by an enhanced hydrocarbon relative permeability. We tested various combinations of oil-stripping effects (M1) and IFT effects (M2) to evaluate the potential impact of each mechanism on the flow behaviour such as the local displacement efficiency, the tracking of tracer flow and the ultimate oil recovery. Oil bypassed by viscous fingering/local heterogeneity, can be efficiently recovered by WAG in the cases where both M1 and M2 are taken into account (as opposed to either mechanism being considered alone). Through tracer analysis, we found that a major recovery mechanism in near-miscible displacement was viscous crossflow between non-preferential (bypassed) flow-paths and preferential flow-paths (i.e. fingers). Indeed this is the key to the recovery of the bypassed oil, which can be strongly amplified/enhanced by the combined mechanisms of M1 and M2 in the case of WAG, but not under continuous CO2 injection alone. This is because during continuous CO2 injection, gas fingers are dominant in the preferential flow paths, and therefore significantly suppress oil flow from the nonpreferential (bypassed) paths into the preferential routes. In contrast, the relatively stable displacing front of WAG is able to make full use of M2, leading to viscous crossflow of bypassed oil into the main preferential flow paths (fingers) and be efficiently produced through M1 by subsequent injections. Eventually, these overall combined mechanisms greatly improve the displacement performance in the case of near-miscible WAG. Due to the significance of IFT effects (M2), we comment on the discrepancy between two of the IFT-dependent relative permeability models (Bette and Coats) and its impact on the simulation of the flow behaviour.

Original languageEnglish
Title of host publicationSPE Reservoir Simulation Conference 2019
PublisherSociety of Petroleum Engineers
ISBN (Electronic)9781613996348
DOIs
Publication statusPublished - 10 Apr 2019
EventSPE Reservoir Simulation Conference 2019 - Galveston, United States
Duration: 10 Apr 201911 Apr 2019

Conference

ConferenceSPE Reservoir Simulation Conference 2019
Abbreviated titleRSC 2019
CountryUnited States
CityGalveston
Period10/04/1911/04/19

Fingerprint

Interfacial Tension
Surface tension
Oils
oil
preferential flow
Injection
gas
permeability
fingering
Recovery
Water
Permeability
tracer
analysis
effect
Path
Air cushion vehicles
water
Cross-flow
Viscous flow

ASJC Scopus subject areas

  • Geochemistry and Petrology
  • Modelling and Simulation

Cite this

Wang, G., Pickup, G., Sorbie, K., Mackay, E., & Skauge, A. (2019). Analysis of near-miscible CO2-WAG displacements: The distinction between compositional and interfacial tension effects. In SPE Reservoir Simulation Conference 2019 [SPE-193907-MS] Society of Petroleum Engineers . https://doi.org/10.2118/193907-MS
@inproceedings{2e98e39c2efe4269bb97b43deab39021,
title = "Analysis of near-miscible CO2-WAG displacements: The distinction between compositional and interfacial tension effects",
abstract = "CO2 Water-Alternating-Gas injection (CO2 WAG), which involves complex phase and flow behaviour, is still a challenging task to simulate and predict accurately. In this paper, we focus specifically on the regime of viscous fingering flow in CO2 WAG in heterogeneous systems because of its importance. We investigated two key physical processes that occur during near-Miscible WAG (nMWAG) processes, namely oil stripping (Mechanism 1, M1) and low-interfacial-tension (IFT) film flow effects (Mechanism 2, M2). The low IFT effects in M2 manifest themselves in an increased mobility of oil phase due to film flow process (discussed below). The importance of properly simulating the interaction of viscous, compositional (M1), and low-interfacial-tension effects (M2) is clearly demonstrated in this study. Our specific aim is to improve the modelling of CO2 displacement in the transition from immiscible to miscible flows in CO2 WAG processes. We simulated both immiscible and near-miscible CO2 WAG and also continuous CO2 displacements with unfavourable mobility ratios for 1D and 2D systems. 2D heterogeneous permeability fields were generated with certain Dykstra-Parsons coefficients and dimensionless correlation ranges. IFT (σgo) was calculated by the simulator as part of the compositional simulation using the McLeod-Sugden equation. The consequent IFT effects on relative permeability was imposed using two commonly used models, i.e. Coats (1980) and Bett{\'e} et al. methods (1991), which have been implemented in many commercial software packages, such as CMG/GEM and E300. Thus, we identify two clear mechanisms of oil recovery that may occur in nearmiscible CO2 (or other gas) injection which we denote as, M1 for oil stripping or compositional effects, and M2 for low-IFT effects which are described by an enhanced hydrocarbon relative permeability. We tested various combinations of oil-stripping effects (M1) and IFT effects (M2) to evaluate the potential impact of each mechanism on the flow behaviour such as the local displacement efficiency, the tracking of tracer flow and the ultimate oil recovery. Oil bypassed by viscous fingering/local heterogeneity, can be efficiently recovered by WAG in the cases where both M1 and M2 are taken into account (as opposed to either mechanism being considered alone). Through tracer analysis, we found that a major recovery mechanism in near-miscible displacement was viscous crossflow between non-preferential (bypassed) flow-paths and preferential flow-paths (i.e. fingers). Indeed this is the key to the recovery of the bypassed oil, which can be strongly amplified/enhanced by the combined mechanisms of M1 and M2 in the case of WAG, but not under continuous CO2 injection alone. This is because during continuous CO2 injection, gas fingers are dominant in the preferential flow paths, and therefore significantly suppress oil flow from the nonpreferential (bypassed) paths into the preferential routes. In contrast, the relatively stable displacing front of WAG is able to make full use of M2, leading to viscous crossflow of bypassed oil into the main preferential flow paths (fingers) and be efficiently produced through M1 by subsequent injections. Eventually, these overall combined mechanisms greatly improve the displacement performance in the case of near-miscible WAG. Due to the significance of IFT effects (M2), we comment on the discrepancy between two of the IFT-dependent relative permeability models (Bette and Coats) and its impact on the simulation of the flow behaviour.",
author = "Gang Wang and Gillian Pickup and Kenneth Sorbie and Eric Mackay and Arne Skauge",
year = "2019",
month = "4",
day = "10",
doi = "10.2118/193907-MS",
language = "English",
booktitle = "SPE Reservoir Simulation Conference 2019",
publisher = "Society of Petroleum Engineers",
address = "United States",

}

Wang, G, Pickup, G, Sorbie, K, Mackay, E & Skauge, A 2019, Analysis of near-miscible CO2-WAG displacements: The distinction between compositional and interfacial tension effects. in SPE Reservoir Simulation Conference 2019., SPE-193907-MS, Society of Petroleum Engineers , SPE Reservoir Simulation Conference 2019, Galveston, United States, 10/04/19. https://doi.org/10.2118/193907-MS

Analysis of near-miscible CO2-WAG displacements : The distinction between compositional and interfacial tension effects. / Wang, Gang; Pickup, Gillian; Sorbie, Kenneth; Mackay, Eric; Skauge, Arne.

SPE Reservoir Simulation Conference 2019. Society of Petroleum Engineers , 2019. SPE-193907-MS.

Research output: Chapter in Book/Report/Conference proceedingConference contribution

TY - GEN

T1 - Analysis of near-miscible CO2-WAG displacements

T2 - The distinction between compositional and interfacial tension effects

AU - Wang, Gang

AU - Pickup, Gillian

AU - Sorbie, Kenneth

AU - Mackay, Eric

AU - Skauge, Arne

PY - 2019/4/10

Y1 - 2019/4/10

N2 - CO2 Water-Alternating-Gas injection (CO2 WAG), which involves complex phase and flow behaviour, is still a challenging task to simulate and predict accurately. In this paper, we focus specifically on the regime of viscous fingering flow in CO2 WAG in heterogeneous systems because of its importance. We investigated two key physical processes that occur during near-Miscible WAG (nMWAG) processes, namely oil stripping (Mechanism 1, M1) and low-interfacial-tension (IFT) film flow effects (Mechanism 2, M2). The low IFT effects in M2 manifest themselves in an increased mobility of oil phase due to film flow process (discussed below). The importance of properly simulating the interaction of viscous, compositional (M1), and low-interfacial-tension effects (M2) is clearly demonstrated in this study. Our specific aim is to improve the modelling of CO2 displacement in the transition from immiscible to miscible flows in CO2 WAG processes. We simulated both immiscible and near-miscible CO2 WAG and also continuous CO2 displacements with unfavourable mobility ratios for 1D and 2D systems. 2D heterogeneous permeability fields were generated with certain Dykstra-Parsons coefficients and dimensionless correlation ranges. IFT (σgo) was calculated by the simulator as part of the compositional simulation using the McLeod-Sugden equation. The consequent IFT effects on relative permeability was imposed using two commonly used models, i.e. Coats (1980) and Betté et al. methods (1991), which have been implemented in many commercial software packages, such as CMG/GEM and E300. Thus, we identify two clear mechanisms of oil recovery that may occur in nearmiscible CO2 (or other gas) injection which we denote as, M1 for oil stripping or compositional effects, and M2 for low-IFT effects which are described by an enhanced hydrocarbon relative permeability. We tested various combinations of oil-stripping effects (M1) and IFT effects (M2) to evaluate the potential impact of each mechanism on the flow behaviour such as the local displacement efficiency, the tracking of tracer flow and the ultimate oil recovery. Oil bypassed by viscous fingering/local heterogeneity, can be efficiently recovered by WAG in the cases where both M1 and M2 are taken into account (as opposed to either mechanism being considered alone). Through tracer analysis, we found that a major recovery mechanism in near-miscible displacement was viscous crossflow between non-preferential (bypassed) flow-paths and preferential flow-paths (i.e. fingers). Indeed this is the key to the recovery of the bypassed oil, which can be strongly amplified/enhanced by the combined mechanisms of M1 and M2 in the case of WAG, but not under continuous CO2 injection alone. This is because during continuous CO2 injection, gas fingers are dominant in the preferential flow paths, and therefore significantly suppress oil flow from the nonpreferential (bypassed) paths into the preferential routes. In contrast, the relatively stable displacing front of WAG is able to make full use of M2, leading to viscous crossflow of bypassed oil into the main preferential flow paths (fingers) and be efficiently produced through M1 by subsequent injections. Eventually, these overall combined mechanisms greatly improve the displacement performance in the case of near-miscible WAG. Due to the significance of IFT effects (M2), we comment on the discrepancy between two of the IFT-dependent relative permeability models (Bette and Coats) and its impact on the simulation of the flow behaviour.

AB - CO2 Water-Alternating-Gas injection (CO2 WAG), which involves complex phase and flow behaviour, is still a challenging task to simulate and predict accurately. In this paper, we focus specifically on the regime of viscous fingering flow in CO2 WAG in heterogeneous systems because of its importance. We investigated two key physical processes that occur during near-Miscible WAG (nMWAG) processes, namely oil stripping (Mechanism 1, M1) and low-interfacial-tension (IFT) film flow effects (Mechanism 2, M2). The low IFT effects in M2 manifest themselves in an increased mobility of oil phase due to film flow process (discussed below). The importance of properly simulating the interaction of viscous, compositional (M1), and low-interfacial-tension effects (M2) is clearly demonstrated in this study. Our specific aim is to improve the modelling of CO2 displacement in the transition from immiscible to miscible flows in CO2 WAG processes. We simulated both immiscible and near-miscible CO2 WAG and also continuous CO2 displacements with unfavourable mobility ratios for 1D and 2D systems. 2D heterogeneous permeability fields were generated with certain Dykstra-Parsons coefficients and dimensionless correlation ranges. IFT (σgo) was calculated by the simulator as part of the compositional simulation using the McLeod-Sugden equation. The consequent IFT effects on relative permeability was imposed using two commonly used models, i.e. Coats (1980) and Betté et al. methods (1991), which have been implemented in many commercial software packages, such as CMG/GEM and E300. Thus, we identify two clear mechanisms of oil recovery that may occur in nearmiscible CO2 (or other gas) injection which we denote as, M1 for oil stripping or compositional effects, and M2 for low-IFT effects which are described by an enhanced hydrocarbon relative permeability. We tested various combinations of oil-stripping effects (M1) and IFT effects (M2) to evaluate the potential impact of each mechanism on the flow behaviour such as the local displacement efficiency, the tracking of tracer flow and the ultimate oil recovery. Oil bypassed by viscous fingering/local heterogeneity, can be efficiently recovered by WAG in the cases where both M1 and M2 are taken into account (as opposed to either mechanism being considered alone). Through tracer analysis, we found that a major recovery mechanism in near-miscible displacement was viscous crossflow between non-preferential (bypassed) flow-paths and preferential flow-paths (i.e. fingers). Indeed this is the key to the recovery of the bypassed oil, which can be strongly amplified/enhanced by the combined mechanisms of M1 and M2 in the case of WAG, but not under continuous CO2 injection alone. This is because during continuous CO2 injection, gas fingers are dominant in the preferential flow paths, and therefore significantly suppress oil flow from the nonpreferential (bypassed) paths into the preferential routes. In contrast, the relatively stable displacing front of WAG is able to make full use of M2, leading to viscous crossflow of bypassed oil into the main preferential flow paths (fingers) and be efficiently produced through M1 by subsequent injections. Eventually, these overall combined mechanisms greatly improve the displacement performance in the case of near-miscible WAG. Due to the significance of IFT effects (M2), we comment on the discrepancy between two of the IFT-dependent relative permeability models (Bette and Coats) and its impact on the simulation of the flow behaviour.

UR - http://www.scopus.com/inward/record.url?scp=85066627703&partnerID=8YFLogxK

U2 - 10.2118/193907-MS

DO - 10.2118/193907-MS

M3 - Conference contribution

BT - SPE Reservoir Simulation Conference 2019

PB - Society of Petroleum Engineers

ER -