乳化剂在反乳化钻井液中的命运:水解和固体吸附

Dimitri M. Khramov, E. Barmatov
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引用次数: 0

摘要

乳化剂浓度是影响钻井液稳定性的重要因素。适当浓度的偕胺胺乳化剂是控制低滤失和保持乳状液稳定性的必要条件。本研究探讨了乳化剂与其他添加剂之间的物理和化学相互作用,并描述了乳化剂从钻井液中去除的过程。乳化剂消耗的三个主要途径是:乳化剂在钻井液和低重力固体(LGS)中的吸附、化学降解和稳定反相乳液。设计了基于1H NMR(核磁共振)谱的实验模型和分析流程,定量研究了非水流体体系(NAF)所需乳化剂浓度。此外,模型系统用于估计乳化剂的过量,评估乳化剂在高温下碱水解造成的损失,并测量乳化剂在重晶石和各种LGS类型上的吸附。基于模型系统的乳化剂消耗计算与配方钻井液的性能相关联,以进行验证。在高性能NAF中,典型的乳化剂需求量为8-12磅/桶。大多数乳化剂被吸附在加重剂(重晶石)和流变性剂(粘土)上,这些物质被用来配制NAF,有助于它们在溶液中有效分散并控制流体流变性。吸附过程对乳化剂浓度、固体矿物学、润湿剂和温度敏感。采用Langmuir-Freundlich等温线对吸附数据进行了描述,并对体系的吸附量进行了估计。乳化剂的降解途径是影响乳化剂消耗量的另一个重要因素;然而,乳化剂在250°F时降解不显著。虽然NAF通常是“富”的,以减轻耗竭和保持流体稳定性,但在矿物上的吸附将成为一个问题,特别是在高LGS浓度下。这些结果将极大地有助于NAF钻井液配方的进一步开发,并将帮助现场工程师了解过量乳化剂对钻井液的影响,使他们能够更有效地控制钻井过程中乳化剂和LGS浓度变化下的流体性质。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Fate of Emulsifier in Invert Emulsion Drilling Fluids: Hydrolysis and Adsorption on Solids
Emulsifier concentration in SBM is an important factor of drilling fluid stability. Proper concentration of amidoamine emulsifier is imperative for controlling low fluid loss and maintaining emulsion stability. This study investigates the physical and chemical interactions between emulsifier and other additives and describes the processes by which emulsifier is depleted from the drilling fluid. Three main pathways of emulsifier consumption are identified: emulsifier adsorption on solids found in drilling fluids and low gravity solids (LGS), chemical degradation, and to stabilize the invert emulsion. Design of experiments model and analytical procedure based on 1H NMR (nuclear magnetic resonance) spectroscopy was used to quantify the required emulsifier concentration in Non-Aqueous Fluid system (NAF). Additionally, model systems were used to estimate the excess of emulsifier, evaluate the emulsifier losses due to alkaline hydrolysis at elevated temperature, and measure adsorption of emulsifier on barite and various LGS types. Calculations for emulsifier depletion based on model systems were correlated to performance of formulated drilling fluids for verification. Typical emulsifier requirement in high performance NAF is 8-12 pounds per barrel (ppb). Majority of the emulsifier is adsorbed on weighting agents (barite) and rheology modifiers (clays), which are used to formulate NAF, that contribute to their effective dispersion in the solution and control fluid rheology. The adsorption process is found to be sensitive to the emulsifier concentration, solids mineralogy, wetting agent and temperature. Analytical Langmuir-Freundlich isotherm was used to describe adsorption data and estimate the adsorption capacity of the system. The emulsifier degradation pathway is another important factor of emulsifier consumption; however, emulsifier degradation at 250°F is not significant. While NAF are generally run ‘rich’ to mitigate depletion and maintain fluid stability, adsorption onto minerals will become an issue especially at high LGS concentration. These results will be greatly beneficial in the further development of NAF drilling fluid formulations and will assist field engineers in understanding the effect excess emulsifier will have on the drilling fluid and enable them to more effectively control the fluid properties under variations in emulsifier and LGS concentration during drilling.
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