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油基高密度钻井液污染解堵液体系

罗志锋 李轲 闫丙森

罗志锋,李轲,闫丙森. 油基高密度钻井液污染解堵液体系[J]. 钻井液与完井液,2025,42(3):418-424 doi: 10.12358/j.issn.1001-5620.2025.03.020
引用本文: 罗志锋,李轲,闫丙森. 油基高密度钻井液污染解堵液体系[J]. 钻井液与完井液,2025,42(3):418-424 doi: 10.12358/j.issn.1001-5620.2025.03.020
LUO Zhifeng, LI Ke, YAN Bingsen.Preparation and application of a block removing fluid for eliminating reservoir contamination by high density oil-based drilling fluids[J]. Drilling Fluid & Completion Fluid,2025, 42(3):418-424 doi: 10.12358/j.issn.1001-5620.2025.03.020
Citation: LUO Zhifeng, LI Ke, YAN Bingsen.Preparation and application of a block removing fluid for eliminating reservoir contamination by high density oil-based drilling fluids[J]. Drilling Fluid & Completion Fluid,2025, 42(3):418-424 doi: 10.12358/j.issn.1001-5620.2025.03.020

油基高密度钻井液污染解堵液体系

doi: 10.12358/j.issn.1001-5620.2025.03.020
详细信息
    作者简介:

    罗志锋,教授,博士,1980年生,2011年毕业于西南石油大学油气田开发工程专业,主要从事油气田增产改造理论与技术研究。E-mail:luozhifeng2022@163.com

  • 中图分类号: TE254.3

Preparation and Application of a Block Removing Fluid for Eliminating Reservoir Contamination by High Density Oil-Based Drilling Fluids

  • 摘要: 油基高密度钻井液因其高度的稳定性和抑制性,在钻井过程中有着广泛的应用,但因其经过滤失、迁移后所形成的重晶石滤饼对储层有着很大的危害,导致油气产量下降。常规化学方法如酸溶,碱溶等方式难以解除滤饼造成的污染。以螯合剂DTPA为主体,添加碳酸钾为转化剂、草酸为催化剂、过硫酸铵为氧化剂,结合以AEC为表面活性剂和乙二醇丁醚为有机溶剂,形成了一套稳定、高效的油基高密度解堵液体系,其对钻井液滤饼渗透、螯合、增溶及洗涤作用,能破坏油基钻井液滤饼内部结构,降低物质间的胶黏作用,增加对油基高密度钻井液污染的解除。高密度钻井液固相螯合液配方为:20%DTPA+3%草酸+6%K2CO3+0.06%过硫酸铵+KOH,油相清洗液的最终配方为:12%乙二醇丁醚+0.5%AEC,对该体系解堵能力,油相清洗能力进行评价。结果表明,在不同的温度条件下(120℃~180℃),复合解堵体系均能对高密度钻井液滤饼有效降解,120℃下单级处理4 h达到66.7%的滤饼溶解率,在120℃多级处理4 h对滤饼的溶解率为72.22%,且滤饼溶解率随温度上升也同时增加,180 ℃多级处理8 h后溶解率为89.24%,最高腐蚀速率为1.1537 g/(m2·h),其具有优秀的解堵性能和耐温性能,在同等实验条件下,复合解堵方法较常规螯合解堵方法对油基钻井液滤饼的溶解效率提升了20%左右,经现场试验证明,该体系能有效解决高密度钻井液所造成的污染及堵塞,其产能恢复率为90%左右。

     

  • 图  1  DTPA浓度与滤饼溶解率的关系

    图  2  草酸浓度与滤饼溶解率的关系

    图  3  K2CO3浓度与滤饼溶解率的关系

    图  4  过硫酸铵浓度与滤饼溶解率的关系

    图  5  解堵液pH值与滤饼溶解率的关系

    图  6  反应时间与滤饼溶解率的关系

    图  7  不同浓度AEC的界面张力

    图  8  不同有机溶剂的去油效率

    图  9  不同浓度乙二醇丁醚溶液的清油能力

    图  10  不同解堵液与地层水配伍性

    图  11  处理方式以及温度与滤饼溶解率的关系

    图  12  A井施工井段(7487.50~7577.00 m)解堵施工曲线

    表  1  添加不同氧化剂的滤饼溶解实验结果

    氧化剂类型 反应前滤饼+
    滤纸质量/g
    反应后滤饼+
    滤纸质量/g
    溶蚀率/
    %
    未添加氧化剂 2.1069 1.6386 47.56%
    0.02%过硫酸铵 2.0757 1.5792 52.42%
    0.02%过硫酸钾 2.1842 1.6381 50.12%
    下载: 导出CSV

    表  2  表面活性剂对接触角的改变程度

    表面
    活性剂
    处理前
    接触角/(°)
    处理后
    接触角/(°)
    接触角
    改变率/%
    AES 105.26 84.77 19.47
    CDEA 98.05 64.19 34.53
    AEC 121.02 69.81 42.32
    下载: 导出CSV

    表  3  不同解堵液常压静态腐蚀实验结果

    液体
    类型
    钢片
    编号
    钢片初
    质量/g
    钢片腐蚀后
    质量/g
    腐蚀速率/
    (g/(m2·h))
    螯合解堵液 739 11.4235 11.4171 1.1537
    清洗液 181 10.9524 10.9521 0.0538
    螯合液+清洗液 340 11.3045 11.3007 0.6882
    下载: 导出CSV
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出版历程
  • 收稿日期:  2024-12-05
  • 修回日期:  2025-02-12
  • 刊出日期:  2025-06-12

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