Modeling analysis of the temperature profile and trapped annular pressure induced by thermal-expanded liquid in a deep gas well

被引:0
作者
Zhang, Bo [1 ]
Zheng, Yushan [1 ]
Deng, Jinrui [1 ]
Lu, Nu [2 ]
Cao, Lihu [3 ]
Wang, Qing [4 ]
Luo, Lihong [5 ]
机构
[1] CNPC, Res Inst Safety & Environm Technol, Beijing, Peoples R China
[2] PetroChina, Res Inst Petr Explorat & Dev, Beijing, Peoples R China
[3] PetroChina, Res Inst Oil & Gas Engn, Tarim Oilfield Co, Korla, Peoples R China
[4] CNPC Engn Technol R&D Co Ltd, Beijing, Peoples R China
[5] CNPC, Bazhou Branch Co, Xibu Drilling Engn Co Ltd, Korla, Peoples R China
关键词
deep gas well; temperature distribution; trapped annular pressure; fluid distribution; mitigation performance; PREDICTION; FAILURE; BUILDUP; INTEGRITY; NITROGEN; BEHAVIOR;
D O I
10.3389/fphy.2022.1014842
中图分类号
O4 [物理学];
学科分类号
0702 ;
摘要
The trapped annular pressure (TAP) caused by thermal expansion is one of the serious challenges for the safe production of a deep gas well. Therefore, this article proposes a model to calculate the temperature profile of the deep gas well based on the heat transfer process and the gas properties. With the help of the temperature model, the TAP in the tubing-casing annulus is analyzed according to the annular fluid distribution and the volume consistence law. The results indicate that the temperature inside the tubing string decreases faster under higher bottom hole pressure. When the tubing-casing annulus is totally filled with the annular protection liquid, the TAP continues increasing with the production rate. Considering the high production rate, the TAP is inevitable and high enough to damage the integrity of the deep gas well. The nitrogen gas mitigates the TAP by reducing the annular liquid volume and providing the extra space to accommodate the thermal-expanded annular liquid. A good mitigation performance can be achieved no matter how large the production rate is. The mitigation performance can be divided into the fastdecreasing stage, the efficient control stage, and the stable stage. These three stages occur as the nitrogen gas column length increases. The compression of the nitrogen gas volume plays a major role in the fast decrease stage while the reduction of the annular liquid plays a major role in the stable stage. For the best cost-effectiveness, the nitrogen gas column is recommended in the efficient control stage and should not exceed 15%.
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页数:9
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