基于压裂添加剂对漏失返排影响的页岩水力压裂设计

A. Al-Ameri, T. Gamadi, I. Ispas, M. Watson
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引用次数: 1

摘要

在整个压裂过程中,注入了数百万加仑的水,但增产后的采收率通常不到50%。本研究旨在评价压裂添加剂对水力压裂返排和漏失的影响。考虑了不同的垫层流体类型,包括;减摩液,减摩液中含有非离子表面活性剂流体和3wt %的盐酸。对Eagle Ford露头岩心样品进行了驱油实验,测量了盐水渗透率、突破时间和水相对渗透率。测量是在完整的样品和用压裂液注入样品后进行的。以页岩储层水力压裂直井为研究对象,建立了模拟扇区模型,研究压裂添加剂对水力压裂返排和漏失的影响。采用敏感性分析方法研究了地层毛管压力和储层压力对逆流毛管吸胀引起的流体返排和失液的影响。研究结果表明,高毛管压力的作用大大降低了近裂缝面页岩基质中的流体饱和度。因此,流体没有从近裂缝面基质返流。此外,在减摩剂垫液中添加非离子表面活性剂或使用3wt %的HCl,可增加泵送过程中的漏失,以及关井、返排和生产过程中的吸吸作用。因此,当压裂面附近基质由于流体饱和度低而没有返排时,建议使用稀HCl酸和较小的关井时间。由于逆流毛管吸胀,近裂缝面区域的失液降低了流体饱和度对产气量的影响。然而,高流体饱和度和聚合物吸附可能导致水堵塞。因此,减少产气量或导致完整的气块。对于毛细管压力适中的页岩,发生了近裂缝面基质的返排。因此,加入非离子表面活性剂和3wt % HCl的减摩剂既增加了逆流毛细吸吸造成的失液,又增加了返排。然而,对于水力压裂,建议使用非离子表面活性剂和长关井时间。储层压力较低的页岩流体返排较少,流体漏失较大。为了最大限度地减少泵送过程中的流体损失并克服水堵问题,建议在垫层阶段使用减摩剂,在随后的压裂步骤中注入非离子表面活性剂或稀酸。
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Hydraulic Fracturing Design in Shale Formations Based on the Impact of Fracturing Additives on the Fluid Loss and Flowback
Throughout fracturing treatment, millions of gallons of water are injected, but commonly less than 50% is recovered after stimulation. This study was constructed to evaluate the impact of the fracturing additives on the fluid flowback and fluid loss during hydraulic fracturing. Different pad fluids types were considered including; friction reducer fluid, friction reducer with a non-ionic surfactant fluid and 3 wt% HCl acid. Flooding experiments were conducted for core samples from the Eagle Ford outcrop to measure the brine permeability, time of breakthrough and water relative permeability. The measurements were performed for intact samples and also after flooding the samples with the fracturing fluids. A simulation sector modeling for a hydraulically fractured vertical well in the shale formation was constructed to investigate the effect of the fracturing additives on the fluid flowback and fluid loss during hydraulic fracturing. A sensitivity analysis was considered to study the effect of the formation capillary pressure and reservoir pressure on the fluid flowback and fluid loss due to counter-current capillary imbibition. The study results showed that the fluid saturation in the near fracture face shale matrix is highly reduced by the effect of the high capillary pressure. Therefore, the fluid had not flow back from the near fracture face matrix. Moreover, adding a non-ionic surfactant to the friction reducer pad fluid or using 3 wt% HCl increased the fluid loss during pumping and the fluid imbibition during shut-in, flowback, and production. Therefore, the dilute HCl acid and small well shut-in times are recommended when no flowback occurs from the near fracture face matrix due to low fluid saturation. The fluid loss from the near fracture face region due to counter-current capillary imbibition reduced the effect of the fluid saturation on the gas production. However, the high fluid saturation and the polymer adsorption may cause water blocks. Thus, reducing the gas production or leading to a complete gas block. For shales with moderate capillary pressure, a flowback from the near fracture face matrix has occurred. Hence, the friction reducer with a non-ionic surfactant fluid and 3 wt% HCl enhanced both of the fluid loss due to counter-current capillary imbibition and the fluid flowback. However, a non-ionic surfactant and long shut-in time are recommended for the hydraulic fracturing. Shales with low reservoir pressure had less fluid flowback and more fluid loss. To minimize the fluid loss during pumping and to overcome the water block problem, it is recommended to use a friction reducer fluid in the pad stage while injecting a non-ionic surfactant or dilute acid during the subsequent fracturing steps.
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