首页> 外文会议>SPE Improved Oil Recovery Conference >Instow a Full Field,Multi-Patterned Alkaline-Surfactant-PolymerFlood-Analyses and Comparison of Phases 1 and 2
【24h】

Instow a Full Field,Multi-Patterned Alkaline-Surfactant-PolymerFlood-Analyses and Comparison of Phases 1 and 2

机译:完整的田间,多图谱碱性表面活性剂 - 聚合物 - 分析和阶段1和2的比较

获取原文

摘要

An Alkaline-Surfactant-Polymer(ASP)project in the Instow field,Upper Shaunavon formation inSaskatchewan Canada was planned in three phases.The first two multi-well pattern phases are nearingcompletion.Beginning in 2007,an ASP solution was injected into Phase 1.Phase 1 polymer drive injectionbegan in 2011 after injection of 35% pore volume(PV)ASP solution.Coincident with the polymer driveinjection into Phase 1,Phase 2 ASP solution injection began.Phase 2 polymer drive began in 2016 afterinjection of 47% PV ASP solution.Polymer drive continues in both phases with Phase 1 and Phase 2 injectedvolume being 55% PV and 35% PV,respectively.Phase 1 and Phase 2 oil cut response to ASP injectionshowed an increase of approximately four times from 3.5% to 12 to 16% and an increase in oil rate fromapproximately 3,200 m3/m(20,000 bbl/m)to 8,300 m3/m(52,000 bbl/m)in Phase 1 and from 2,200 m3/m(14,000 bbl/m)to 7,800 m3/m(49,000 bbl/m)in Phase 2.Phase 1 pattern analysis indicates the pore volumesof ASP solution injected varied from 13% to 54% PV of ASP with oil recovery percentage increasing withincreasing injected volume.Oil recoveries in the different patterns ranged from 3% OOIP up to 21% OOIPwith lower oil recoveries correlating with lower volume of ASP injected.The response from some of thepatterns correlates with coreflood results.Wells in common to the two phases show increase oil cut and oilrate responses to chemical injection from both Phases 1 and 2.Oil recovery as of August 2019 is 60% OOIPfor Phase 1 and 57% OOIP for Phase 2.Phase 1 economic analysis indicated chemical and operation costwould be approximately C$26/bbl resulting in the decision to move forward with Phase 2.
机译:在储存领域的碱性表面活性剂 - 聚合物(ASP)项目,上少春形成insaskatchewan加拿大计划分三相。前两种多孔模式阶段接近Completion.beginning,将ASP溶液注入第1期。第1阶段聚合物驱动注射液在2011年注射35%孔体积(PV)ASP溶液后。用聚合物软射入相1,相2 ASP溶液注射突出开始.20P2聚合物驱动开始于2016年的47%PV ASP溶液。 。共聚物驱动器在两个相中继续相位1和相2的注射尺,分别为55%PV和35%PV,分别为ASP注射的25%的抗液,其增加约4倍至12%至12%至12%至12%至16%增加储油率为3,200m 3 / m(20,000bbl / m)至8,300m 3 / m(52,000bbl / m),2,200 m 3 / m(14,000 bbl / m)至7,800m 3 / m(49,000 BBL / M)在第2阶段1模式分析表明孔径孔径注入的溶液在asp的13%至54%pv时,具有油回收率的增加,增加了注射体积的含量。不同图案中的回收率范围为3%ooip,高达21%ooipwith较低的油回收与较低体积的asp的较低的asp。响应来自一些本地与CoreFlood结果相关联。两种阶段共同的威尔威尔斯显示,截至2019年8月的两种阶段和2阶段恢复,增加油切口和对化学注射的反应是60%oOIP的液相1和57%oop阶段2.双相1经济分析表明化学和运营费用约为26美元/ BBL,导致阶段第2阶段前进的决定。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号