A new pressure control scheme on steam‐assisted gravity drainage for heavy oil production

Author:

Jia Xinfeng1,Wang Kangkang12,Xiong Jian1,Jiao Binhai1,Liu Dong3,Chen Zhangxin14,Jiang Liangliang4,Pang Zhanxi1

Affiliation:

1. School of Petroleum Engineering China University of Petroleum Beijing China

2. Changqing Oilfield Company China National Petroleum Corporation Xi'an China

3. Tianjin Branch China National Offshore Oil Corporation Tianjin China

4. Schulich School of Engineering University of Calgary Calgary Alberta Canada

Abstract

AbstractAs one the most important recovery mechanisms of steam‐assisted gravity drainage (SAGD), gravity drainage is largely dependent on the inclination angle of the steam chamber edge. The existence of solution‐gas causes an ellipsoid‐shaped chamber that has small inclination angle at the bottom, which leads to inefficient gravity drainage and slows down oil production. To address this problem, this study proposes a new scheme, variable‐pressure SAGD (VP‐SAGD). It is basically a SAGD process, at certain stages of which pressure surge is induced by controlling the operating conditions so that the shape of steam chamber can be altered. This leads to a larger slip angle in the steam chamber at the bottom and more efficient heat transport between hot steam and crude oil. Results show that VP‐SAGD is able to increase oil recovery by up to 20% and decrease cumulative steam–oil ratio (cSOR) by up to 7%. Its special oil extraction mechanisms include swabbing effect, enlarged inclination angle of steam chamber boundary at the bottom, and enhanced heat transfer. Particularly, the inclination angle is increased by up to 40%. In addition, a lower producer bottom‐hole pressure (BHP) during pressure drawdown leads to a better production incremental in later stages. The optimal timing for pressure surge is the middle stage of steam chamber growth. The lower the producer BHP decrease, the better the yield increase. Moreover, The VP‐SAGD strategy works better in heavy oil reservoirs with a permeability of k = 0.5–10 Darcy or solution gas content of greater than 2%.

Funder

China University of Petroleum, Beijing

National Natural Science Foundation of China

Publisher

Wiley

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