原位支撑剂:珠状支撑剂、微支撑剂和通道支撑剂

Jiangshui Huang, Wei Gong, Lijun Lin, C. Yin, Fu-Chen Liu, Han Zhou, Litao Bai, Lulu Song, Zhengzhou Yang
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引用次数: 3

摘要

致密油储层需要增产才能开采出圈闭油。油气行业最常用的增产措施是水力压裂。压裂作业往往会产生裂缝,包括主裂缝和微裂缝。本研究的目的是开发一种压裂液,该压裂液可以在压裂作业中就地转化为微支撑剂、微珠和通道支撑剂,以提高微裂缝和主裂缝的水力导流能力,并简化水力压裂作业,其中通道支撑剂被定义为被通道包围的柱。树脂、固化剂、表面活性剂和水相混合在一起形成O/W乳液,作为压裂液。固化后,树脂与固化剂在原位反应形成支撑剂。研究了影响支撑剂形成的参数,如固化温度、压力、混合强度、表面活性剂浓度和粒径控制添加剂,从而通过控制参数,可以按要求在原位形成微支撑剂、微珠和通道支撑剂。测试了其粒径分布、球形度、圆度、电导率、酸溶解度和抗压强度。通过控制实验参数和加入粒径控制添加剂,压裂液可以在30 ~ 90℃的温度范围内按要求转化为微支撑剂、微珠和通道支撑剂,树脂和固化剂几乎100%转化为支撑剂,比密度为1.09g/ml。小球的球形度和圆度均超过0.9,在加载至15 kpsi后产生的细粒小于2%,酸溶解度为2.37%,在室温下,在4000 psi的支撑剂加载1 lb/ft2的情况下,小球的电导率为227 mD-ft。微支撑剂的球形度和圆度均接近于1,d50约为80µm。此外,在玻璃板制成的人工裂缝中形成了通道支撑剂。因此,随着压裂液的开发,可以通过原位形成通道化支撑剂和微支撑剂来最大限度地优化井的导流能力,从而分别保持主裂缝和微裂缝的张开。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
In-situ Proppant: Beads, Microproppant, and Channelized-Proppant
Tight oil reservoirs need stimulation in order to produce the trapped oil. The most common form of stimulation used by the oil and gas industry is hydraulic fracturing. Fracturing operations tend to create fractures including primary fractures and microfractures. The objective of this study is to develop a fracturing fluid which can be converted into microproppant, beads, and channelized-proppant as desired in-situ during a fracturing operation to enhance the hydraulic conductivity of the microfractures and the primary fractures, and simplify the hydraulic fracturing operation, where the channelized-proppant is defined as the pillars surrounded by channels. Resin, curing agents, surfactants, and aqueous phase were mixed together to form O/W emulsion to serve as fracturing fluid. After curing process, resin and curing agent would react and form proppant in-situ. The parameters affect the proppant formation such as the curing temperatures, pressure, mixing strength, surfactant concentration, and size control additives were all studied and thus through controlling the parameters, microproppant, beads, and channelized-proppant can form in-situ as desired. The particle size distribution, sphericity, roundness, conductivity, acid solubility, and crush strength were tested. Through controlling the experimental parameters and adding size control additives, fracturing fluid can be converted into microproppant, beads, and channelized-proppant as desired at a temperature from 30° C to 90° C. Almost 100% of the resin and the curing agents were converted into proppant with a specific density of 1.09g/ml. For the beads, both the sphericity and roundness are over 0.9, less than 2% fines were generated after being loaded to 15 kpsi, the acid solubility is 2.37%, and the conductivity of the beads of 20/40 mesh tested with proppant loading of 1 lb/ft2 at 4000 psi at room temperature was 227 mD-ft. For the microproppant, both the sphericity and roundness are close to 1 with d50 about 80 µm. Furthermore, channelized-proppant was formed in an artificial fracture with walls made of glass sheets. Thus, with the fracturing fluid developed, the conductivity of the well can be maximally optimized through the in-situ formation of channelized proppant and microproppant to keep the primary fractures and microfractures open respectively.
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