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一种耐高温长效自生酸酸液体系的制备与性能研究

李明轩,  姚奕明,  陈晨,  李大奇,  吴雄军

李明轩,姚奕明,陈晨,等. 一种耐高温长效自生酸酸液体系的制备与性能研究[J]. 钻井液与完井液,2026,43(5):702-710 doi: 10.12358/j.issn.1001-5620.2026.05.015
引用本文: 李明轩,姚奕明,陈晨,等. 一种耐高温长效自生酸酸液体系的制备与性能研究[J]. 钻井液与完井液,2026,43(5):702-710 doi: 10.12358/j.issn.1001-5620.2026.05.015
Li Mingxuan, Yao Yiming, Chen Chen, et al.Synthesis and performance evaluation of a high-temperature resistant long-acting self-generated acid fluid system[J]. Drilling Fluid & Completion Fluid,2026, 43(5):702-710 doi: 10.12358/j.issn.1001-5620.2026.05.015
Citation: Li Mingxuan, Yao Yiming, Chen Chen, et al.Synthesis and performance evaluation of a high-temperature resistant long-acting self-generated acid fluid system[J]. Drilling Fluid & Completion Fluid,2026, 43(5):702-710 doi: 10.12358/j.issn.1001-5620.2026.05.015

一种耐高温长效自生酸酸液体系的制备与性能研究

doi: 10.12358/j.issn.1001-5620.2026.05.015
基金项目: 国家重大专项项目“多功能型压裂液体系与高性能材料研发”(2024ZD1404702);中国石化科技部攻关课题“塔里木盆地万米深井完井改造关键技术研究及工程应用”(P24157)。
详细信息
    作者简介:

    李明轩,助理研究员,博士,1993年生,毕业于中国石油大学(华东)化学专业,现在从事酸化压裂技术研究工作。E-mail:limx0613.sripe@sinopec.com

    通讯作者:

    姚奕明,研究员,现在从事酸化压裂方面的研究工作。E-mail:yaoym.sripe@sinopec.com。

  • 中图分类号: TE357.12

Synthesis and Performance Evaluation of a High-Temperature Resistant Long-Acting Self-Generated Acid Fluid System

  • 摘要: 针对深层高温碳酸盐岩储层酸化改造中,常规酸液反应过快而现有自生酸生酸强度低、耐温性不足的问题,研发了一种新型耐高温生酸剂SFACA,并据此构建了耐高温长效自生酸酸液体系。实验结果表明,SFACA基于“活化-水解-解离-循环催化”的高效生酸机制,可在60 ℃~180 ℃温度范围内持续释放离子,并在140 ℃以上激发高效生酸活性,有效氢离子浓度可达7.8 mol·kg−1,且通过优化剂/水质量比可实现酸浓度的灵活调控。基于SFACA所构建的自生酸酸液体系配伍性良好,对碳酸盐岩主矿物CaCO3表现出高效溶蚀能力,在160 ℃和180 ℃下的酸岩有效作用时间分别达7 h和4 h,酸岩反应速率分别为1.45×10−7 mol·cm−2·s−1和2.46×10−7 mol·cm−2·s−1,具备长效作用特性。此外,该酸液在160 ℃和180 ℃下对N80钢片的动态腐蚀速率分别为56.3 g·m−2·h−1和67.8 g·m−2·h−1,具有良好的缓蚀性能。该自生酸酸液体系实现了高温条件下的高酸度、长效缓释与高效溶蚀,能够为160 ℃~180 ℃深层高温碳酸盐岩储层的高效改造提供可靠的技术支撑。

     

  • 图  1  不同温度下有效氢离子浓度随时间变化曲线

    图  2  不同温度下酸液有效溶蚀率随时间的变化曲线

    图  3  自生酸生酸与溶蚀反应机理示意图

    图  4  动态腐蚀前后钢片形貌

    表  1  不同剂/水比条件下SFACA水解实验结果

    序号 碳酸钙溶
    蚀量/g
    等效盐酸
    浓度/%
    转化率/
    %
    剂/水
    质量比
    1 6.97 25.9 89.3 1∶0.1
    2 7.67 23.7 98.3 1∶0.2
    3 7.81 20.3 100.0 1∶0.4
    4 7.82 19.2 100.1 1∶0.8
    5 7.81 16.2 99.9 1∶1.0
    6 7.82 11.4 100.1 1∶1.5
    7 7.80 6.9 99.9 1∶2.5
    下载: 导出CSV

    表  2  岩样初始岩矿成分分析

    矿物组分 CaCO3 SiO2 Al2O3 Fe2O3 其他杂质
    质量分数/% 96.5 2.1 0.8 0.4 0.2
    下载: 导出CSV

    表  3  不同酸液体系反应前后岩样成分变化

    酸液类型T/
    ℃
    矿物组分/%
    CaCO3SiO2Al2O3Fe2O3其他杂质
    20%盐酸1600.658.523.512.25.2
    1800.359.824.211.54.2
    自生酸1600.858.923.511.75.1
    1800.559.923.711.24.7
    下载: 导出CSV

    表  4  选择性溶蚀定量分析结果

    酸液类型T/
    ℃
    CaCO3溶蚀率/
    %
    难溶矿物富集系数
    20%盐酸16099.428.6
    18099.728.9
    自生酸16099.228.5
    18099.528.7
    下载: 导出CSV

    表  5  酸岩反应动力学参数测试结果

    序号 测试温度/
    ℃
    酸岩反应速率/
    ×10−7 mol·cm−2·s−1
    表观活化能/
    kJ·mol−1
    1 160 1.45 44.3
    2 180 2.46
    下载: 导出CSV

    表  6  不同温度下缓蚀性能评价结果

    腐蚀类型 酸液体系 T/
    ℃
    P/
    MPa
    缓蚀剂/
    %
    平均腐蚀速率/
    g·m−2·h−1
    静态腐蚀 20%盐酸 90 0.1 0.5 23.90
    自生酸 0.5 1.35
    动态腐蚀 20%盐酸 160 16.0 4.0 69.20
    自生酸 4.0 56.30
    20%盐酸 180 16.0 5.0 78.50
    自生酸 5.0 67.80
    下载: 导出CSV
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  • 收稿日期:  2026-02-09
  • 修回日期:  2026-03-11
  • 录用日期:  2026-03-22
  • 刊出日期:  2026-10-01

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