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    使用水力屏障控制单一倾斜储层中CO2羽的迁移

    赵锐锐 成建梅

    赵锐锐, 成建梅, 2016. 使用水力屏障控制单一倾斜储层中CO2羽的迁移. 地球科学, 41(4): 675-682. doi: 10.3799/dqkx.2016.056
    引用本文: 赵锐锐, 成建梅, 2016. 使用水力屏障控制单一倾斜储层中CO2羽的迁移. 地球科学, 41(4): 675-682. doi: 10.3799/dqkx.2016.056
    Zhao Ruirui, Cheng Jianmei, 2016. Using Hydraulic Barrier Control CO2 Plume Migration in Sloping Reservoir. Earth Science, 41(4): 675-682. doi: 10.3799/dqkx.2016.056
    Citation: Zhao Ruirui, Cheng Jianmei, 2016. Using Hydraulic Barrier Control CO2 Plume Migration in Sloping Reservoir. Earth Science, 41(4): 675-682. doi: 10.3799/dqkx.2016.056

    使用水力屏障控制单一倾斜储层中CO2羽的迁移

    doi: 10.3799/dqkx.2016.056
    基金项目: 

    国家自然科学基金项目 41402212

    中央高校基本科研业务费专项资金资助项目 CUGL140814

    国家自然科学基金项目 1172217

    详细信息
      作者简介:

      赵锐锐(1984-),男,讲师,主要从事CO2地质封存和地下水数值模拟技术方面的研究工作.E-mail: rr.zhao@cug.edu.cn

      通讯作者:

      成建梅,E-mail: jmcheng@cug.edu.cn

    • 中图分类号: P641

    Using Hydraulic Barrier Control CO2 Plume Migration in Sloping Reservoir

    • 摘要: 摘要:在单一倾斜含水层中封存CO2时,在浮力作用下,CO2会向地层上升一侧快速运移,不利于封存安全.可在倾斜地层的上升一侧,距离CO2注入井一定位置设置注水井,创造水力屏障,以阻止CO2向上移动.建立了数值模型来探讨这一方法的有效性,分析注水位置、距离、速度等因素的影响.结果表明注水形成的水力屏障能有效阻挡CO2羽的向上迁移,且能促进CO2溶解,抽水能显著降低地层压力.为了确保能完全阻挡CO2运移,需要注水长度大于CO2羽的厚度,甚至是在全部储层注水.注水速度是影响水力屏障效果的关键因素.注水距离越近阻挡效果越好.可以在CO2羽即将到达之前注水,以减少注水量和能源消耗.

       

    • 图  1  模型三维视图

      Fig.  1.  The three-dimensional view of the model

      图  2  模型示意

      Fig.  2.  The sketch of the model

      图  3  Base case中A-A′剖面CO2饱和度和溶解的质量分数在不同时间的分布情况

      剖面位置见图 1Sg代表CO2饱和度;XCO2代表CO2溶解的质量分数

      Fig.  3.  The distribution of CO2 gas saturation and dissolved CO2 mass fraction along the A-A′ cross section at different times for the Base case

      图  4  Case 1a和Case 1c中A-A′剖面CO2饱和度在不同时间的分布情况

      剖面位置见图 1Sg代表CO2饱和度

      Fig.  4.  The distribution of CO2 gas saturation along the A-A′ cross section at different times for the Cases 1a and 1c

      图  5  Case 2a和Case 2b中A-A′剖面CO2饱和度在50 a时的分布情况

      剖面位置见图 1Sg代表CO2饱和度

      Fig.  5.  The distribution of CO2 gas saturation along the A-A′ cross section at 50 years for the Cases 2a and 2b

      图  6  Case 3a和Case 3c中A-A′剖面CO2饱和度在不同时间的分布情况

      剖面位置见图 1Sg代表CO2饱和度

      Fig.  6.  The distribution of CO2 gas saturation along the A-A′ cross section at different times for the Cases 3a and 3c

      图  7  Case 4a和Case 4b中A-A′剖面CO2饱和度在100年时的分布情况

      剖面位置见图 1Sg代表CO2饱和度;XCO2代表CO2溶解的质量分数

      Fig.  7.  The distribution of CO2 gas saturation along the A-A′ cross section at 100 years for the Cases 4a and 4b

      图  8  不同抽水速度下监测点的压力提升情况

      Fig.  8.  The pressure buildup of the monitoring point at different injection rates

      表  1  模型主要参数取值

      Table  1.   The values of main model parameters

      地层 Kh (10-15 m2) Kh/Kv α-1(MPa) β(10-10 Pa-1) Srw Srg m
      盖层 0.001 10 5.00 4.5 0.40 0.15 0.457
      储层 100 10 0.02 4.5 0.30 0.15 0.457
      注:Kh为水平渗透率;Kh/Kv为水平和垂直渗透率的比值;α-1为毛细进入压力;β为压缩率;Srw为最大残余水饱和度;Srg为最大残余气饱和度;m为相对渗透率函数中的指数.
      下载: 导出CSV

      表  2  不同注水方案中的参数设置

      Table  2.   The parameter values used in the different injection scenarios

      方案编号 注水位置 注水距离(km) 注水速度(kg/s) 停止注入CO2后注水速度(kg/s) 抽水速度(kg/s)
      Base case 全部储层 1 31.7 10 31.7
      Case 1a 储层上部100 m
      Case 1b 储层上部40 m
      Case 1c 储层上部20 m
      Case 2a 2
      Case 2b 3
      Case 2c 5
      Case 3a 10.0
      Case 3b 5.0
      Case 3c 1.0
      Case 4a 5
      Case 4b 1
      Case 5a 10.0
      Case 5b 5.0
      Case 5c 0(不抽水)
      注:空白处与Base case设置相同.
      下载: 导出CSV
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    • 收稿日期:  2015-09-08
    • 刊出日期:  2016-04-15

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