T. Yushchenko, E. V. Demin, R. Khabibullin, K. S. Sorokin, Mikhail Viktorovich Khachaturyan, I. V. Baykov, R. I. Gatin
{"title":"Operation Features of Wells with an Extended Horizontal Wellbore and Multistage Hydraulic Fracturing Operation in Bazhenov Formation","authors":"T. Yushchenko, E. V. Demin, R. Khabibullin, K. S. Sorokin, Mikhail Viktorovich Khachaturyan, I. V. Baykov, R. I. Gatin","doi":"10.2118/206482-ms","DOIUrl":null,"url":null,"abstract":"\n Wells with extended horizontal wellbore (HW) drilling with multistage hydraulic fracturing (MHF) is necessary for commercial oil production from Bazhenov formation (Vashkevich et al., 2015; Strizhnev, 2019). Today the maximum HW length for Bazhenov formation wells is 1500 m (Strizhnev, 2019, Korobitsyn et al., 2020). In international practice the maximum HW length for shale oil production is around 3000-400 m (Rodionova et al., 2019). Pump Down Perforator (PDP) technology is used for MHF: a liner is run in hole and cemented, then perforation and hydraulic fracturing (HF) are successively performed by stages at equal distances from the end to the beginning of HW to create a branched system of fractures in Bazhenov formation. Performed HF stages are isolated with special packer plugs (insoluble blind, dissolvable blind, insoluble with seat for dissolvable ball or dissolvable with seat for dissolvable ball)) (Mingazov et al., 2020). Consequently, the fluid inflow into the well is occurred along whole HW and the flow rate increases from monotonically from the end to the beginning of HW and has maximum value at last HF stage. The numbers of HF stages are about 24-30 (number of perforating clusters - 100) at one well in Russia and 50 in the world (Alzahabi et al., 2019).\n One of important parameter during HF is the speed of HF fluid injection into the formation. Tubing outer diameters 114-140 mm. are used in HW to increase the injection rate and reduce friction losses in the well. The flow rate of HF fluid in this case reach to 14-16 m3/min (Ogneva et al., 2020; Astafiev et al., 2015). Monobore wells construction is planned to use with outer diameter 140 mm. A stinger is used as sealing element between tubing and liner to minimizing risk of HF liquids leaks into the annulus (Astafiev et al., 2015). As a result, the inner well diameter from wellhead to bottomhole is around constant in the process of MHF.\n The pressure in the hydraulic fractures and the collector near fractures after MHF is highly exceeded the initial reservoir pressure. Hence wellhead pressure after MHF in water filled well is about 100-150 bar (Jing Wang et al., 2021). This fact significantly limits downhole well operations because of requires killing (tubing change, let down ESP, etc.). These works are required heavy well killing fluid because of high overpressure. It is undesirable because of it can reduce the fracture conductivity, worse well bottom zone properties and reduce well productivity. Therefore, the well is working at flowing mode in initial period usually until the reservoir pressure in the drainage area is decreased at the hydrostatic level or below (Jing Wang et al., 2021). After that the well can be killing using technical water with a density of 1.01 – 1.07 g/sm3 (the use of well-killing fluid with a density higher than 1.1 g/sm3 is undesirable). The possibility of well flowing working depends on properties of collector and reservoir fluid: High gas-oil ratio (GOR) and reservoir conductivity help well flowing until reservoir pressure drop off hydrostatic pressure.","PeriodicalId":11177,"journal":{"name":"Day 4 Fri, October 15, 2021","volume":"202 1","pages":""},"PeriodicalIF":0.0000,"publicationDate":"2021-10-12","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Day 4 Fri, October 15, 2021","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.2118/206482-ms","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0
Abstract
Wells with extended horizontal wellbore (HW) drilling with multistage hydraulic fracturing (MHF) is necessary for commercial oil production from Bazhenov formation (Vashkevich et al., 2015; Strizhnev, 2019). Today the maximum HW length for Bazhenov formation wells is 1500 m (Strizhnev, 2019, Korobitsyn et al., 2020). In international practice the maximum HW length for shale oil production is around 3000-400 m (Rodionova et al., 2019). Pump Down Perforator (PDP) technology is used for MHF: a liner is run in hole and cemented, then perforation and hydraulic fracturing (HF) are successively performed by stages at equal distances from the end to the beginning of HW to create a branched system of fractures in Bazhenov formation. Performed HF stages are isolated with special packer plugs (insoluble blind, dissolvable blind, insoluble with seat for dissolvable ball or dissolvable with seat for dissolvable ball)) (Mingazov et al., 2020). Consequently, the fluid inflow into the well is occurred along whole HW and the flow rate increases from monotonically from the end to the beginning of HW and has maximum value at last HF stage. The numbers of HF stages are about 24-30 (number of perforating clusters - 100) at one well in Russia and 50 in the world (Alzahabi et al., 2019).
One of important parameter during HF is the speed of HF fluid injection into the formation. Tubing outer diameters 114-140 mm. are used in HW to increase the injection rate and reduce friction losses in the well. The flow rate of HF fluid in this case reach to 14-16 m3/min (Ogneva et al., 2020; Astafiev et al., 2015). Monobore wells construction is planned to use with outer diameter 140 mm. A stinger is used as sealing element between tubing and liner to minimizing risk of HF liquids leaks into the annulus (Astafiev et al., 2015). As a result, the inner well diameter from wellhead to bottomhole is around constant in the process of MHF.
The pressure in the hydraulic fractures and the collector near fractures after MHF is highly exceeded the initial reservoir pressure. Hence wellhead pressure after MHF in water filled well is about 100-150 bar (Jing Wang et al., 2021). This fact significantly limits downhole well operations because of requires killing (tubing change, let down ESP, etc.). These works are required heavy well killing fluid because of high overpressure. It is undesirable because of it can reduce the fracture conductivity, worse well bottom zone properties and reduce well productivity. Therefore, the well is working at flowing mode in initial period usually until the reservoir pressure in the drainage area is decreased at the hydrostatic level or below (Jing Wang et al., 2021). After that the well can be killing using technical water with a density of 1.01 – 1.07 g/sm3 (the use of well-killing fluid with a density higher than 1.1 g/sm3 is undesirable). The possibility of well flowing working depends on properties of collector and reservoir fluid: High gas-oil ratio (GOR) and reservoir conductivity help well flowing until reservoir pressure drop off hydrostatic pressure.
对于Bazhenov地层的商业采油来说,采用扩展水平井眼(HW)钻井和多级水力压裂(MHF)是必要的(Vashkevich等,2015;Strizhnev, 2019)。目前Bazhenov地层井的最大井长为1500米(Strizhnev, 2019, Korobitsyn等,2020)。在国际实践中,页岩油开采的最大HW长度约为3000-400 m (Rodionova et al., 2019)。泵下射孔器(PDP)技术用于MHF:将尾管下入井中并固井,然后依次进行射孔和水力压裂(HF),从HW的末端到开始,以相同的距离分段进行,在Bazhenov地层中形成分支裂缝系统。已完成的HF级使用特殊封隔器桥塞(不溶性盲塞、可溶性盲塞、可溶球不溶性阀座或可溶球可溶阀座)进行隔离(Mingazov等,2020)。因此,井内流体沿整个HF阶段流入,从HF阶段结束到HF阶段开始,流量呈单调递增趋势,在HF阶段末达到最大值。俄罗斯一口井的高频级数约为24-30级(射孔簇数量为100个),世界上为50级(Alzahabi等人,2019)。高频流体注入地层的速度是高频流体注入地层的一个重要参数。油管外径114-140 mm用于HW,以提高注入速度并减少井中的摩擦损失。在这种情况下HF流体的流量达到14-16 m3/min (Ogneva et al., 2020;Astafiev et al., 2015)。计划采用外径140mm的单孔井施工。推力杆用作油管和尾管之间的密封元件,以最大限度地降低HF液体泄漏到环空的风险(Astafiev等,2015)。因此,在MHF过程中,从井口到井底的内井直径基本保持恒定。MHF后水力裂缝内和裂缝附近集热器内的压力大大超过了初始储层压力。因此,充水井中MHF后的井口压力约为100-150 bar (Jing Wang et al., 2021)。由于需要压井(换油管、下放电潜泵等),这极大地限制了井下作业。由于高压,这些作业需要使用重型压井液。这是不可取的,因为它会降低裂缝导流能力,使井底层性能变差,降低油井产能。因此,井在初始阶段通常处于流动状态,直到泄放区储层压力降至静水水平或以下(Jing Wang et al., 2021)。之后,可以使用密度为1.01 - 1.07 g/sm3的技术水进行压井(不希望使用密度高于1.1 g/sm3的压井液)。井筒流动工作的可能性取决于捕集剂和储层流体的性质:高气油比(GOR)和储层导电性有助于井筒流动,直到储层压力低于静水压力。