超深井气举管柱力学动态响应及失效风险评价OA
Mechanical dynamic response and failure risk evaluation of pipe strings during gas lift in ultra-deep wells
超深井通常伴随高温、高压及高含硫化氢、二氧化碳等腐蚀性介质的环境,套管在长期服役过程中有可能受到不同程度的腐蚀损伤,其气举过程因温度、压力波动与腐蚀损伤耦合作用易导致油套管柱失效,需要建立一套综合考虑多相流瞬态压力、腐蚀缺陷及非线性力学行为的管柱安全评价方法.为此,采用有限体积法建立包含气举流态、井筒结构、流体参数及封隔器泄漏的气举瞬态多相流模型,结合非线性有限元法构建了基于风险点压力分布的腐蚀套管三维力学模型,进而形成了气举过程中腐蚀套管安全评价图版,并结合环空动态压力建立了系统性的风险评价方法.研究结果表明:①开始注气及气举过程中环空最大压力位于封隔器上方(井深6 213.78 m),达86.5 MPa;停止注气后环空最大压力转移至油管鞋处(井深6 401.9 m),分别为83.4 MPa(积液未排完)与60.9 MPa(积液排完).②在温度为156℃,腐蚀半径为0.5~4.5 mm,环空压力为55~110 MPa的条件下,腐蚀半径与环空压力增大均会增加H140套管安全风险,其中环空压力的影响更为突出,实际作业中应重点监测其波动情况.③所构建的安全评价图版与风险评价方法可有效评估不同气举阶段及地层压力衰减程度下在役腐蚀套管的安全系数.结论认为,该项研究成果为超深井气举过程工艺参数优化及管柱风险评价提供了依据.
Ultra-deep wells are typically in the environments with high temperature,high pressure,and high concentrations of corrosive media such as hydrogen sulfide and carbon dioxide.During long-term service,casings are subjected to varying degrees of corrosion damage.The gas lift process,due to the coupling effects of temperature and pressure fluctuations with corrosion damage,can easily lead to the failure of tubing and casing strings.Therefore,it is necessary to establish a set of safety evaluation methods for pipe strings that consider transient multiphase flow pressures,corrosion defects,and nonlinear mechanical behaviors comprehensively.In this paper,a transient multiphase flow model of gas lift is developed using the finite volume method.The model involves gas lift flow patterns,wellbore geometry,fluid parameters,and packer leakage.Then,a three-dimensional mechanical model of corroded casing based on risk point pressure distribution is constructed by means of the nonlinear finite element method.On this basis,the safety evaluation charts for corroded casings during gas lift operations are developed.Finally,a systematic risk assessment method is constructed on the basis of annular dynamic pressure.The following results are obtained.First,during gas injection initiation and the gas lift process,the maximum annular pressure appears at a position above the packer(6 213.78 m),reaching 86.5 MPa.After gas injection stops,the maximum annular pressure transfers to the tubing shoe(6 401.9 m),and it is 83.4 MPa(with incomplete liquid unloading)and 60.9 MPa(with complete liquid unloading).Second,when the corrosion radius is 0.5-4.5 mm and the annular pressure is 55-110 MPa,the increase in corrosion radius and annular pressure at 156℃ can elevate the safety risk of H140 casing,with annular pressure having a more pronounced impact.During actual operations,therefore,monitoring focus should be put on the fluctuation of annular pressure.Third,the developed safety evaluation charts and risk assessment method can effectively evaluate the safety factors of in-service corroded casings under different gas lift stages and varying degrees of in-situ stress attenuation.The research findings provide a theoretical basis for optimizing process parameters and assessing pipe string risks during gas lift operations in ultra-deep wells.
邓宽海;王俊杰;叶富铭;杨刘;姚明远;Sinan Ihsan AL-Shaibani;曾德智;张敬逸;刘乔平
西南石油大学||中国石油天然气集团有限公司石油管工程重点实验室(西南石油大学)西南石油大学||中国石油天然气集团有限公司石油管工程重点实验室(西南石油大学)中国石油西南油气田公司重庆气矿西南石油大学||中国石油天然气集团有限公司石油管工程重点实验室(西南石油大学)西南石油大学||中国石油天然气集团有限公司石油管工程重点实验室(西南石油大学)伊拉克石油部石油研发中心西南石油大学||中国石油天然气集团有限公司石油管工程重点实验室(西南石油大学)振华石油控股有限公司中石化重庆涪陵页岩气勘探开发有限公司
能源科技
超深井气举管柱力学动态响应多相流模拟动态压力安全评价评价方法
Ultra-deep wellGas liftPipe string mechanicsDynamic responseMultiphase flow simulationDynamic pressureSafety evaluationAssessment method
《天然气工业》 2026 (2)
113-123,11
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