高压、高温、盐度条件下CO2泡沫螯合增产液的流变性优化

Ahmed BinGhanim, Jawad Al-Darweesh, M. Aljawad, Xianmin Zhou, M. Kamal, Zuhair AlYousif, M. Mahmoud
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引用次数: 4

摘要

泡沫酸性流体由于其各种优点,已被用于提高石油采收率和压裂应用。增强返排、回收处理液和降低每次操作的总用水量都是这些优势的例子。本研究考察了l -谷氨酸- n, n -二乙酸(GLDA)螯合剂在N2和CO2泡沫流体中的应用,提高了泡沫酸性流体的稳定性,降低了腐蚀倾向,并且对环境友好。采用改进的高压高温(HPHT)泡沫流变仪和环境条件下的泡沫分析仪,对N2和CO2在采出水中制备的酸性泡沫流体进行了测试。筛选出的烷基二胺衍生物表面活性剂在212-300°F和1000 psi下进行了测试,有和没有GLDA。研究了缓蚀剂的加入对粘度和泡沫质量的影响。粘度和泡沫质量测量是在增加剪切速率从5001 /s到20001 /s的情况下进行的。结果表明,GLDA提高了泡沫流体的粘度和稳定性。结果表明,高剪切速率下黏度为5cp,低剪切速率下黏度为25cp。粘度,一般来说,降低较高的剪切速率,但泡沫质量不受影响。含有缓蚀剂的流体体系也可以降低粘度。表面活性剂浓度为1 wt.%, GLDA添加量为15 wt.%,不添加缓蚀剂时,粘度值相对较高且最稳定。环境条件泡沫分析仪结果显示,使用N2泡沫的泡沫高度和半衰期分别为182.8 mm和16.5分钟,而使用CO2泡沫的泡沫高度和半衰期分别为77.4 mm和2.16分钟。在所有情况下,缓蚀剂的加入都对CO2泡沫流体的半衰期有显著的负面影响,但对半衰期影响最小。所提供的流变学研究没有考虑增稠剂的加入,增稠剂可以进一步研究。本文研究了一种螯合剂在恶劣条件下作为CO2和N2酸性泡沫流体添加剂的新应用。此外,测试的流体系统可以在高达300°F的温度下作为可靠的增产流体系统进行研究和利用。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Rheological Optimization of CO2 Foamed Chelating Stimulation Fluids at High-Pressure, High-Temperature, and Salinity
Foamed acidic fluids have been utilized in the industry for enhanced oil recovery and fracturing applications due to their various advantages. Flowback enhancement, recovery of treatment fluids, and reduction of overall water consumption per operation are examples of these advantages. This study examines the utilization of a chelating agent, L-glutamic acid-N, N-diacetic acid (GLDA) in N2 and CO2 foamed fluids, which enhances the stability of foamed acidic fluids, lowers corrosion tendency, and is environmentally friendly. A modified high pressure and high temperature (HPHT) foam rheometer, and foam analyzer at ambient conditions, are used to test the acidic foamed fluids prepared in produced water using N2 and CO2. A screened out Alkyl diamine derivative surfactant has been tested at 212-300 °F and 1000 psi with and without GLDA. The effect of corrosion inhibitor addition on viscosity and foam quality is also investigated. Viscosity and foam quality measurements were done at increasing shear rates from 500 1/s up to 2000 1/s. Results showed that GLDA enhances the foamed fluid viscosity and stability. Resulted viscosities were in the range of 5 cP at higher shear rates to 25 cP in the lower shear rates region. Viscosity, in general, is lowered by higher shear rates, but foam quality is not affected. Fluid systems with a corrosion inhibitor also resulted in lower viscosities. The most stable and relatively higher viscosity values resulted from the 1 wt.% surfactant concentration with the addition of 15 wt.% GLDA and no corrosion inhibitor. Ambient conditions foam analyzer results showed higher foam height and half-life values of 182.8 mm and 16.5 minutes respectively when foaimg using N2 compared to 77.4 mm and 2.16 minutes when foamed with CO2. The addition of corrosion inhibitor showed significant negative impact in all cases, but least on the half-life of the CO2 foamed fluid. The rheology study provided did not consider the addition of thickeners which could be further investigated. This study covers the novel utilization of a chelating agent as an additive in CO2 and N2 acidic foamed fluids at harsh conditions. Furthermore, the fluid systems tested can be investigated and utilized as reliable stimulation fluid systems at temperatures up to 300 °F.
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