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SPE Members Abstract A compositional reservoir simulation evaluation' of the Brassey Artex B Pool, located in British Columbia, Canada, was undertaken to predict hydrocarbon recoveries under a variety of development schemes. The subject reservoir is a thin aeolian sand containing a volatile, highly undersaturated oil. A miscible flood was initiated in 1989 immediately following delineation drilling. The numerical model was constructed using the most up-to-date geological, geophysical, and petrophysical data. Surface facilities were incorporated into the model, through the use of individual well test separators for production tests performed prior to implementation of a miscible flood, and by a four-stage separator after implementation of the miscible flood. This model was then calibrated by history matching three years of volumetric and compositional data. Tracer survey results were also used in the model calibration phase. Reservoir fluid compositions were represented in the model with a nine pseudo-component Peng-Robinson equation of state. The equation of state was calibrated to laboratory constant composition expansion, differential liberation, swelling test, and slim tube data to provide representative PVT properties of the reservoir fluid and injected solvent. The history matched model was then used to forecast the production performance for a variety of production and injection schemes, including infill drilling and sensitivities to injected solvent composition. The reservoir fluid characterization phase of the study verified that the recovery process was one of first-contact miscibility at the 4000 psia operating pressure. Analysis of the pressure, saturation, and fluid composition distributions demonstrated that an effective first-contact miscible displacement was occurring in the reservoir. While the majority of the pool will be swept with the existing well configuration, two infill drilling locations have been identified. Phase behaviour analysis indicated that the current injection gas is richer than required to achieve first contact miscibility; therefore, liquids can be extracted and sold from the injection gas stream. History matching of the compositional model suggested an initial oil in place volume approximately one-third less than that derived from previous pseudo-miscible black oil studies. However, the initial analytical material balance estimates derived from production tests conducted prior to the miscible flood showed an oil in place volume midway between the two model estimates. This comparison highlighted the difficulties of characterizing the volumetric behaviour of near-critical fluids using either compositional or black oil techniques. Introduction The Brassey field, located in northeastern British Columbia, was discovered in 1979 with the drilling of the d-89-B/93-P-10 well (Figure 1). Test results showed the well to be in a limited reservoir, and no further drilling was done until 1987, when the d-71-C/93-P-10 well encountered the overpressed Artex member of the Triassic Charlie Lake formation. Delineation drilling followed over the ensuing two years, with seven oil-production wells and four gas-injection wells being drilled into the Artex B Pool, the largest of several Artex pools in the field and the subject of this paper. Due to the strongly oil-wet nature of the reservoir rock, concerns over water compatibility with the anhydrite present in the zone, and the very undersaturated oil, the decision was made to move directly to a miscible hydrocarbon gas injection development after delineation drilling. The final well configuration was five-spot injection pattern with wells on 320-acre spacing. P. 339^
SPE Members Abstract A compositional reservoir simulation evaluation' of the Brassey Artex B Pool, located in British Columbia, Canada, was undertaken to predict hydrocarbon recoveries under a variety of development schemes. The subject reservoir is a thin aeolian sand containing a volatile, highly undersaturated oil. A miscible flood was initiated in 1989 immediately following delineation drilling. The numerical model was constructed using the most up-to-date geological, geophysical, and petrophysical data. Surface facilities were incorporated into the model, through the use of individual well test separators for production tests performed prior to implementation of a miscible flood, and by a four-stage separator after implementation of the miscible flood. This model was then calibrated by history matching three years of volumetric and compositional data. Tracer survey results were also used in the model calibration phase. Reservoir fluid compositions were represented in the model with a nine pseudo-component Peng-Robinson equation of state. The equation of state was calibrated to laboratory constant composition expansion, differential liberation, swelling test, and slim tube data to provide representative PVT properties of the reservoir fluid and injected solvent. The history matched model was then used to forecast the production performance for a variety of production and injection schemes, including infill drilling and sensitivities to injected solvent composition. The reservoir fluid characterization phase of the study verified that the recovery process was one of first-contact miscibility at the 4000 psia operating pressure. Analysis of the pressure, saturation, and fluid composition distributions demonstrated that an effective first-contact miscible displacement was occurring in the reservoir. While the majority of the pool will be swept with the existing well configuration, two infill drilling locations have been identified. Phase behaviour analysis indicated that the current injection gas is richer than required to achieve first contact miscibility; therefore, liquids can be extracted and sold from the injection gas stream. History matching of the compositional model suggested an initial oil in place volume approximately one-third less than that derived from previous pseudo-miscible black oil studies. However, the initial analytical material balance estimates derived from production tests conducted prior to the miscible flood showed an oil in place volume midway between the two model estimates. This comparison highlighted the difficulties of characterizing the volumetric behaviour of near-critical fluids using either compositional or black oil techniques. Introduction The Brassey field, located in northeastern British Columbia, was discovered in 1979 with the drilling of the d-89-B/93-P-10 well (Figure 1). Test results showed the well to be in a limited reservoir, and no further drilling was done until 1987, when the d-71-C/93-P-10 well encountered the overpressed Artex member of the Triassic Charlie Lake formation. Delineation drilling followed over the ensuing two years, with seven oil-production wells and four gas-injection wells being drilled into the Artex B Pool, the largest of several Artex pools in the field and the subject of this paper. Due to the strongly oil-wet nature of the reservoir rock, concerns over water compatibility with the anhydrite present in the zone, and the very undersaturated oil, the decision was made to move directly to a miscible hydrocarbon gas injection development after delineation drilling. The final well configuration was five-spot injection pattern with wells on 320-acre spacing. P. 339^
Miscible flooding was invented many years ago, and in the 1950's it was viewed as one of the most promising techniques to use for improving oil recovery from a reservoir.1,2,3,4,5,6,7 Since that time many groups have researched what would be the most important parameters to optimize in the lab, have developed theoretical models to correlate these parameters, and then have implemented these "optimally designed" gas injection systems in the field. Amidst all the increase in technology and sophistication there is still ongoing debate as to whether one needs to achieve miscibility in order to optimize the recovery or whether a degree of immiscibility, characterized by the name "near miscible", is equally adequate for field implementation in enhanced oil recovery processes. This paper seeks to provide insight into these questions by reviewing some of the parameters which are at work in gas injection EOR as well as qualifying some of the techniques which can be used in designing gases for injection. Moreover, case histories are described herein where laboratory work was performed, phase behavior described, and then the gas injected into the reservoir. Results from the field are then shown and commentary included on the field performance.
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