化工学报 ›› 2018, Vol. 69 ›› Issue (S1): 58-63.DOI: 10.11949/j.issn.0438-1157.20180776

• 流体力学与传递现象 • 上一篇    下一篇

多孔介质内超临界CO2流体及泡沫驱油特性的比较实验研究

杜东兴1,2, 郑利晨1,2, 张旭1,2, 孙国龙1,2, 李莺歌3, 巢昆1,2   

  1. 1 青岛科技大学机电工程学院, 山东 青岛 266061;
    2 青岛科技大学地质能源研究院, 山东 青岛 266109;
    3 青岛科技大学自动化与电子工程学院, 山东 青岛 266061
  • 收稿日期:2018-07-10 修回日期:2018-07-17 出版日期:2018-09-30 发布日期:2018-09-30
  • 通讯作者: 杜东兴(1971-),男,博士研究生,教授,E-mail:du-dongxing@163.com
  • 基金资助:

    国家自然科学基金项目(51476081)。

Comparative experimental studies on oil recovery characteristics of supercritical CO2 and foam fluid in porous media

DU Dongxing1,2, ZHENG Lichen1,2, ZHANG Xu1,2, SUN Guolong1,2, LI Yingge3, CHAO Kun1,2   

  1. 1 College of Electromechanical Engineering, Qingdao University of Science and Technology, Qingdao 266061, Shandong, China;
    2 Geo-Energy Research Institute, Qingdao University of Science and Technology, Qingdao 266109, Shandong, China;
    3 College of Automation and Electronic Engineering, Qingdao University of Science and Technology, Qingdao 266061, Shandong, China
  • Received:2018-07-10 Revised:2018-07-17 Online:2018-09-30 Published:2018-09-30
  • Supported by:

    supported by the National Natural Science Foundation of China (51476081).

摘要:

CO2混相驱替可以提高原油采收率,因此近年来得到研究者们的广泛关注。使用高温高压驱替设备,利用超临界CO2流体、超临界CO2泡沫及N2泡沫作为驱替介质,对油水饱和孔隙介质中的油相驱替特性开展了比较实验研究。通过对驱替过程沿程压力及对驱替增采油量的测量,对不同驱替手段在孔隙介质内的油相增采特性进行深入研究和探讨。研究发现在温度为50℃、压力为13 MPa时,超临界CO2流体对多孔介质内的油相驱替效果有显著提升,当压力进一步升高到23 MPa时,油相增采效果不明显。说明在本实验条件下超临界CO2流体与油相在50℃、13 MPa时可达到混相驱替状态;而采用超临界CO2泡沫及N2泡沫注入工艺未能进一步提高出油量。沿程压差测量结果则显示,与N2泡沫相比,超临界CO2泡沫在多孔介质试样内的驱替压差较小,起泡性能较差。实验结果对于筛选及评价超临界CO2驱油工艺具有一定的指导意义。

关键词: 超临界二氧化碳, 泡沫, 多相流, 驱油特性

Abstract:

CO2 miscible displacement process has attracted wide attention of researchers in recent years due to its capacity on enhancing oil recovery. Comparative experimental investigations were carried out for oil recovery characteristics from water/oil pre-saturated porous medium with various displacement fluids of supercritical CO2, supercritical CO2 foam and N2 foam. Referring to the reservoir temperature and pressure conditions, the enhanced oil recovery characteristics are analyzed and discussed in detail based on the displacement pressure drop along the core together with the extracted amount of oil from the porous medium. It is found the supercritical CO2 fluid could achieve obviously higher oil recovery at the condition of 50℃ and 13 MPa. The fact that elevating the system pressure up to 23 MPa couldn't produce extra oil indicates the CO2 displacing oil process achieves miscibility under the condition of 50℃ and 13 MPa in the porous media. The employments of other EOR methods of supercritical CO2 foam and N2 foam didn't produce more oil component from the sample. Compared to the result of 0.8 MPa for N2 foam, the pressure drop for supercritical CO2 foam flooding process is much lower at 0.3 MPa with poorer bubble generation performance. It is expected the experimental results could be employed on screening and evaluating supercritical CO2 flooding technologies.

Key words: supercritical carbon dioxide, foam, multiphase flow, oil recovery characteristics

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