纳米颗粒注入介质在提高采收率中的应用进展

Muhammad Arshad, K. Feilberg, A. Shapiro, K. Thomsen
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引用次数: 0

摘要

本文介绍了矿物碳酸钙CaCO3(即方解石和文石)两种不同多晶型的晶体形态对乳化液热稳定性的影响,以及一项后续研究(基于我们之前在Arshad et al., 2018a中报道的乳化液表征工作)。采用不同盐浓度的卤水(去离子水(DIW)、合成海水(0.5SSW和SSW)、地层水(FW2和FW1)、模拟油(癸烷(D)和1:1体积比的正己烷-十六烷(HH))和北海原油(NSCO)样品。采用方解石细粒(粒径≤30 μm)、文石细粒(粒径≤5 μm)和方解石纳米粒3种不同粒径(15-40、50和90 nm)在盐水-油混合物中形成乳状液。利用扫描电镜(SEM)和透射电镜(TEM)对CaCO3微米级颗粒(方解石和文石)和纳米方解石进行了表征。采用x射线粉末衍射(XRD)对方解石和文石细粒的晶体结构进行了表征。布兰森Sonifier®SFX250(强制乳化)用于在盐水油颗粒/纳米颗粒中生成乳液。用光学显微镜(Axio Scope.A1)表征乳状液滴的大小。乳剂的热稳定性分为两个阶段进行测试,首先将乳剂在室温下保存12-23个月(乳剂相读数分别在第1周、第5个月、第12个月和第23个月),然后在定制的封闭水浴中在80°C的高温下加热40天。晶体形貌研究表明,虽然方解石细粒(≤30 μm)的尺寸是文石细粒(≤5 μm)的6倍,但在DIW-HH混合物中,方解石细粒(≤30 μm)产生的乳化液量较大,乳化液滴相对较小。这表明细颗粒的晶体形态是影响乳化液形成和乳化液尺寸的主要因素,而不是细颗粒的大小,因此在选择用于提高采收率的纳米颗粒时,应将晶体形态作为重要参数加以考虑。在盐水盐度(DIW、0.5SSW、SSW、FW2和FW1)、油类型(D、HH和NSCO)和方解石纳米颗粒尺寸(15-40、50和90 nm)的不同范围内,研究了盐水-油-方解石纳米颗粒的乳状液热稳定性。所有卤水- d -方解石纳米颗粒体系在室温下12个月和80℃高温下40天均表现出优异的热稳定性。在所有卤水- d -方解石纳米颗粒的情况下,观察到0.5SSW-D-CaCO3体系中50 nm方解石纳米颗粒的最大累计破乳率为6%(从第5个月到80°C加热40天)。由于正己烷的沸点较低(~ 68℃),因此在80℃下没有对卤水- hh -方解石纳米颗粒体系进行测试。他们在室温下进行了长达23个月的测试,所有研究的系统都表现出优异的热稳定性,从第5个月到第23个月,乳液相没有可测量的变化。在卤水- nsco -方解石纳米颗粒体系中,15-40 nm和90 nm尺寸的纳米颗粒在室温下表现出优异的热稳定性,在80℃时表现出很好的热稳定性。与15-40 nm和90 nm纳米颗粒的结果相反,50 nm纳米颗粒在本研究中测试的整个盐水盐度范围内表现出较差的热稳定性。在所有被研究的体系中,在80°C下加热40天,乳化相的减少幅度最大,为39%(对于SSW-NSCO-CaCO3体系)。同样,在所有被研究的体系中,FW2-NSCO-CaCO3体系(从室温第1周到80℃加热40天)的累计破乳率最大,为47.5%。研究还发现,与DIW体系相比,体系中盐(SSW、FW2和FW1)的存在提高了乳液在室温和80°C下的热稳定性(50 nm纳米颗粒除外)。在这项工作中,具有不同晶体形态的颗粒的乳液形成行为以及乳液在长时间和高温下的热稳定性对开发基于纳米颗粒的EOR应用非常有益。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Development of Nanoparticles as Injection Media in Enhanced Oil Recovery
The effect of crystal morphology of two different polymorphs of mineral calcium carbonate, CaCO3, (i.e., calcite and aragonite) and a follow-up study (based on our previous work on emulsion characterization as reported in Arshad et al., 2018 a) on the thermal stability of emulsions are presented in this work. Brines with varying salt concentration (deionized water (DIW), synthetic seawater (0.5SSW and SSW), and formation water (FW2 and FW1)), model oils (decane (D) and 1:1 vol. ratio of hexane–hexadecane (HH)), and a sample of North Sea crude oil (NSCO) were employed. Calcite fines (size ≤ 30 μm), aragonite fines (size ≤ 5 μm), and calcite nanoparticles of three different sizes (15–40, 50, and 90 nm) were used for emulsion formation in brine–oil mixtures. CaCO3 micron-sized fines (calcite and aragonite) and calcite nanoparticles were characterized by Scanning Electron Microscope (SEM) and Transmission Electron Microscope (TEM), respectively. X-ray Powder Diffraction (XRD) was performed to examine the crystal structure of calcite and aragonite fines. Branson Sonifier® SFX250 (forced emulsification) was employed for emulsion generation in brine–oil–fines/nanoparticles. An optical microscope (Axio Scope.A1) was used for characterizing the emulsion droplet size. Thermal stability of the emulsions was examined in two stages, first by keeping them at room temperature for an extended period of 12–23 months (emulsion phase readings were taken at week–1, month–5, month–12, and month–23) followed by heating them at an elevated temperature of 80 °C for a period of 40 days in a custom-made closed water bath. The crystal morphology study showed that although the calcite fines (≤ 30 μm) were six times bigger in size in comparison to the aragonite fines (≤ 5 μm), they generated a comparatively large amount of emulsion with relatively smaller emulsion droplets in the DIW–HH mixtures. This indicates that the crystal morphology of fines was the dominating factor in emulsion formation and emulsion droplet size instead of the size of fines and the crystal morphology should be considered as an important parameter in the selection of nanoparticles for EOR applications. Emulsion thermal stability was examined in brine–oil–calcite nanoparticles with a wide range of brine salinity (DIW, 0.5SSW, SSW, FW2, and FW1), oil type (D, HH, and NSCO), and size of calcite nanoparticles (15–40, 50, and 90 nm). All the brine–D–calcite nanoparticles systems showed excellent thermal stability both at room temperature for 12 months and at an elevated temperature of 80 °C for 40 days. Amongst all the brine–D–calcite nanoparticles cases, a maximum cumulative de-emulsification (from month–5 to heating at 80 °C for 40 days) of 6 % was observed for the 0.5SSW–D–CaCO3 system with 50 nm calcite nanoparticles. Due to the lower boiling temperature of hexane (~ 68 °C), the brine–HH–calcite nanoparticles systems were not tested at 80 °C. They were instead tested at room temperature for an extended period of up to 23 months and all the studied systems showed excellent thermal stability with no measurable change in the emulsion phase from month–5 to month–23. In case of the brine–NSCO–calcite nanoparticles systems, nanoparticles with 15–40 and 90 nm sizes generally showed excellent thermal stability at room temperature and very good thermal stability at 80 °C. Contrary to the results of nanoparticles with 15–40 and 90 nm sizes, 50 nm nanoparticles exhibited poor thermal stability for the whole rage of brine salinity tested in this work. They showed the largest reduction in the emulsion phase of 39 % (for the SSW–NSCO–CaCO3 system) when heated at 80 °C for 40 days amongst all the studied systems. Similarly, the FW2–NSCO–CaCO3 system showed the largest cumulative (from week–1 at room temperature to heating at 80 °C for 40 days) de-emulsification of 47.5 % amongst all the studied systems. It was also observed that the presence of salts in the system (SSW, FW2, and FW1) promoted thermal stability of the emulsions compared to the DIW system, both at room temperature and at 80 °C (with an exception of 50 nm nanoparticles). Emulsion formation behavior of particles with different crystal morphology and emulsion thermal stability over an extended period and at an elevated temperature as presented in this work can be very beneficial in developing nanoparticles based EOR applications.
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