批量反应系统中膦酸盐阻垢剂的耦合吸附/沉淀模型

M. K. Meybodi, K. Sorbie, O. Vazquez, K. Jarrahian, E. J. Mackay
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引用次数: 0

摘要

阻垢剂挤压处理是防止水垢沉积的最常见方法之一。如果产水中的阻垢剂(SI)浓度高于某个阈值,即最小阻垢剂浓度(MIC),矿物垢就会被抑制。因此,通过吸附(Γ)和沉淀(Π)对 SI 的滞留进行精确建模对于成功设计和实施挤压处理至关重要。本研究建立了一个平衡模型,用于模拟膦酸盐阻垢剂在钙镁阳离子存在下,在碳酸盐等活性地层中的吸附-沉淀(Γ/Π)耦合过程。在这种方法中,阻垢剂 (SI) 被视为一种多弱酸,可能会被质子化 (HnA),从而与钙/镁离子发生络合反应,导致 SI_Ca/Mg 复合物沉淀。所有这些反应都发生在一个综合系统中,碳酸盐系统反应和可溶性物质的吸附同时进行。在吸附过程中,所有残留在溶液中的 SI 衍生物,包括游离和复合物种,都被认为参与了吸附过程,吸附等温线模型(如 Freundlich)对此进行了描述。对于沉淀部分,该模型考虑了以下反应:(i) 碳酸盐系统,(ii) SI(被认为是弱多酸的 HnA)标本,(iii) SI-金属(钙和镁)结合复合物,以及 (iv) SI-Ca/Mg 复合物的后续沉淀。考虑到系统电荷平衡以及钙、镁、碳和 SI 的质量平衡,通过数值求解一组确定的非线性方程,对系统(不包括吸附物种)进行数值平衡。在对方程进行代数还原后,系统简化为三个非线性方程,可以用牛顿-拉斐森方法求解。根据实验室实验确定的 SI 在溶液中的溶解度,在平衡模型中模拟了 SI-Ca/Mg 的沉淀。通过与之前一项研究(Kalantari Meybodi 等人,2023 年)中关于 DETPMP 在方解石/盐水(含游离 Ca/Mg)体系中的相互作用的实验结果进行比较,确定了所提模型的可靠性,其中对 SI、Ca2+、Mg2+、CO2 和 pH 的最终浓度进行了比较。建模结果显示与实验结果基本吻合,并进行了进一步的敏感性分析,以研究一些不确定参数的行为,如络合物的稳定常数。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Coupled Adsorption/Precipitation Modelling of Phosphonate Scale Inhibitors in a Batch Reactive System
Scale inhibitor squeeze treatments are one of the most common ways to prevent scale deposition. The mineral scale will be inhibited if the concentration of the scale inhibitor (SI) in the produced water is above a certain threshold, known as the Minimum Inhibitor Concentration (MIC), which is controlled by scale inhibitor retention. Therefore, accurate modelling of the SI retention through adsorption (Γ) and precipitation (А) is critical to the successful design and implementation of squeeze treatments. In this study, an equilibrium model has been developed to simulate the coupled adsorption-precipitation (Ð/А) of phosphonate scale inhibitors in reactive formations, such as carbonates, in the presence of calcium and magnesium cations. In this approach, the scale inhibitor (SI) was considered as a poly weak acid that may be protonated (HnA), resulting in the complexation with Ca/Mg ions, leading to the precipitation of SI_Ca/Mg complexes. All these reactions occur in an integrated system where carbonate system reactions and adsorption of the soluble species are occurring in parallel. In the adsorption process, all the SI derivatives remaining in the solution, including free and complex species, are considered to participate in the adsorption process, described by an an adsorption isotherm model (e.g., Freundlich). For the precipitation part, the model considers the following reactions: (i) the carbonate system, (ii) SI speciation, considered as weak polyacid, HnA, (iii) the SI-metal (Ca and Mg) binding complexes, and (iv) subsequent precipitation of the SI-Ca/Mg complex. The system charge balance and the mass balances for calcium, magnesium, carbon, and SI are considered, to numerically equilibrate the system (excluding the adsorbed species), by solving a determined set of non-linear equations numerically. Following the algebraic reduction of the equations, the system is reduced to three non-linear equations that may be solved by the Newton-Raphson method. The precipitation of the SI-Ca/Mg is modelled in the equilibrium model based on the solubility of SI in the solution, determined from the lab experiments. The reliability of the proposed model was established by comparison with experimental results from a previous study (Kalantari Meybodi et al., 2023) on the interactions of DETPMP in a Calcite/brine (containing free Ca/Mg) system, where the final concentration of SI, Ca2+, Mg2+, CO2 and pH were compared. The modelling showed good general agreement with the experimental results, and a further sensitivity analysis was performed to examine the behaviour of some uncertain parameters, such as the stability constant of complexes.
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