樊彬,邓济平,毛崇昊,等. 煤层气水平井中气锚失效机理[J]. 石油钻采工艺,2026,48(1):133-138. DOI: 10.13639/j.odpt.202509018
引用本文: 樊彬,邓济平,毛崇昊,等. 煤层气水平井中气锚失效机理[J]. 石油钻采工艺,2026,48(1):133-138. DOI: 10.13639/j.odpt.202509018
FAN Bin, DENG Jiping, MAO Chonghao, et al. Failure mechanism of gas anchors in coalbed methane horizontal wells[J]. Oil Drilling & Production Technology, 2026, 48(1): 133-138. DOI: 10.13639/j.odpt.202509018
Citation: FAN Bin, DENG Jiping, MAO Chonghao, et al. Failure mechanism of gas anchors in coalbed methane horizontal wells[J]. Oil Drilling & Production Technology, 2026, 48(1): 133-138. DOI: 10.13639/j.odpt.202509018

煤层气水平井中气锚失效机理

Failure mechanism of gas anchors in coalbed methane horizontal wells

  • 摘要: 重力型气锚在煤层气水平井中应用效果差,油管连续出气问题严重。为研究其失效机理,搭建了一套高11 m、与水平方向呈6°倾角、带螺杆泵和可视化气锚的排液采气实验装置。使用高速摄像机分别监测气锚内部和油管出口气液两相流态,以观察到油管连续出气作为气锚失效的依据,开展不同螺杆泵转速100~300 r/min、气相流量100~1 100 m3/d、井底压力150~300 kPa的气锚失效实验。水平井筒中,气锚通过内部液相分隔油套环空和螺杆泵进液口,以实现环空中气液两相的分离,气锚的排液速度大于进液速度是其失效的原因。螺杆泵转速为200 r/min、气相流量为400 m3/d时,气相仅以气泡形式进入气锚;提高螺杆泵转速到300 r/min,气锚内交界面下降到进液口下方,环空气相直接与泵连通,气锚失效。降低螺杆泵转速、优化气锚进液口形状和增加气锚深度都能提高气锚失效的气相流量。研究结果对煤层气井生产制度调节和气锚工具改进具有指导意义。

     

    Abstract: The gravitational gas anchor performs poorly in coalbed methane horizontal wells, with severe continuous gas production through the tubing. To clarify its failure mechanism, a liquid drainage and gas production experimental setup was constructed. It is 11 m high, inclined at 6° to the horizontal, and equipped with a progressing cavity pump (PCP) and a visual gas anchor. A high-speed camera was used to monitor the gas-liquid two-phase flow patterns inside the gas anchor and at the tubing outlet. Continuous gas production through the tubing was taken as the criterion for gas anchor failure. Experiments on gas anchor failure were conducted under different PCP rotational speeds 100~300 r/min, gas flow rates 100~1 100 m3/d, and bottomhole pressures 150~300 kPa. In the horizontal well, the gas anchor separates the annular space of the oil ring and the inlet of the screw pump through internal liquid phase separation to achieve the separation of gas-liquid two-phase in the annular space. The failure of the gas anchor occurs when its liquid discharge rate exceeds its liquid intake rate. At a PCP speed of 200 r/min and a gas flow rate of 400 m3/d, gas enters the anchor only in the form of bubbles. When the PCP speed is increased to 300 r/min, the gas-liquid interface inside the anchor drops below the inlet, allowing direct gas flow from the annulus into the pump and resulting in anchor failure. Reducing the PCP rotational speed, optimizing the shape of the gas anchor inlet, and increasing the depth of the gas anchor can all raise the gas flow rate at which failure occurs. The findings provide guidance for adjusting production strategies and improving gas anchor design in CBM wells.

     

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