“…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).…”