2015
DOI: 10.1016/j.petrol.2015.04.005
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Analysis of steam–solvent–bitumen phase behavior and solvent mass transfer for improving the performance of the ES-SAGD process

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Cited by 45 publications
(15 citation statements)
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References 56 publications
(69 reference statements)
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“…In SAGD, as shown in Figure 2b, the region near the steam chamber edge is divided into three zones: the steam condensation zone, in which steam condenses upon contacting cold oil sands; the mobile oil zone, located in the vicinity and ahead of the steam chamber edge, containing mobilized oil and water; and the immobile oil zone, far from the chamber edge, which is at initial oil sands conditions. 27 It is assumed that the steam chamber is equilibrated at saturation pressure (P st ) and temperature (T st ), and that the chamber edge (a condensation front) propagates toward the cold oil sands reservoir (downstream, at the right side of this region). Ahead of the steam chamber edge, a varying temperature zone is formed with hot liquids flowing in the lateral (x) direction.…”
Section: Model Descriptionmentioning
confidence: 99%
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“…In SAGD, as shown in Figure 2b, the region near the steam chamber edge is divided into three zones: the steam condensation zone, in which steam condenses upon contacting cold oil sands; the mobile oil zone, located in the vicinity and ahead of the steam chamber edge, containing mobilized oil and water; and the immobile oil zone, far from the chamber edge, which is at initial oil sands conditions. 27 It is assumed that the steam chamber is equilibrated at saturation pressure (P st ) and temperature (T st ), and that the chamber edge (a condensation front) propagates toward the cold oil sands reservoir (downstream, at the right side of this region). Ahead of the steam chamber edge, a varying temperature zone is formed with hot liquids flowing in the lateral (x) direction.…”
Section: Model Descriptionmentioning
confidence: 99%
“…In this model, the target region of thickness, h , is surrounded by permeable oil sands, above and below (which enables liquid flow by gravity drainage), initially saturated with oil ( S oi ) and water ( S wi ), and is at initial oil sands temperature ( T ini ) and pressure ( P ini ). In SAGD, as shown in Figure b, the region near the steam chamber edge is divided into three zones: the steam condensation zone, in which steam condenses upon contacting cold oil sands; the mobile oil zone, located in the vicinity and ahead of the steam chamber edge, containing mobilized oil and water; and the immobile oil zone, far from the chamber edge, which is at initial oil sands conditions . It is assumed that the steam chamber is equilibrated at saturation pressure ( P st ) and temperature ( T st ), and that the chamber edge (a condensation front) propagates toward the cold oil sands reservoir (downstream, at the right side of this region).…”
Section: Model Descriptionmentioning
confidence: 99%
“…Steam-assisted gravity drainage (SAGD) is commonly used to develop extraheavy oil reservoirs [2,3]. Nevertheless, the low utilization rate and high-energy loss of the SAGD process are major problems, which result in its limited application [4]. The production efficiency of the SAGD is low, and the cost of the production process is high [5].…”
Section: Introductionmentioning
confidence: 99%
“…The physical properties of the reservoir are generally not the main constraints in fire flooding development. The main constraint in fire flooding is the viscosity of the heavy oil [7][8][9][10][11][12][13][14][15]. Unlike most other countries that conduct fire flooding in reservoirs with formation oil viscosities of less than 5000 mPa•s, the viscosity of the heavy oil in some fire flooding test areas in China can reach 20000 mPa•s.…”
Section: Introductionmentioning
confidence: 99%