模拟挤压处理/示踪剂程序设计

O. Vazquez, I. Giannakouras, E. Mackay
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引用次数: 0

摘要

在设计挤压处理时,最大的挑战之一是确保在完井段中适当地投放化学药剂。一般来说,化学段塞是头状的;因此,在长水平井和/或横流井中,将化学品暴露在所有完井段可能很困难。本文介绍了一种评价布局效率的方法。如果放置不当,井的某些部分将不受保护,从而导致不希望出现的情况:由于表面测量到的抑制剂回流浓度高于阈值,井可能看起来受到了保护,但由于未接触化学药剂的井区域结垢而导致生产损失。在这种情况下,可以通过生产测井准确地确定抑制剂的位置,但这可能会非常昂贵。另一种选择是使用示踪剂来评估层流率分布,从而量化化学物质的放置。本文的目的是确定示踪剂包是否可以在具有挑战性的井中作为挤压处理的一部分,特别是在溢流阶段。如果井筒中存在压力不同的区域,那么以不同的速率将示踪剂递进生产,将导致示踪剂返回浓度曲线具有特征特征,可以解释为估计化学物质的放置。考虑了两种具有横流的三层情况。在这两种情况下,溢出中都包含了一个跟踪程序包,结果返回的概要文件清楚地显示了所需的特性。这种方法的主要优点是操作费用不会显著增加。唯一的额外费用将是特定示踪剂和后续分析的费用。预计该成本低于挤压处理总成本的5%。在注入示踪剂后,这种新型的多速率挤压后生产阶段的结果表明,在挤压处理中包含这种示踪剂包是可行的。收集到的数据可用于优化后续处理的设计,以确保通过控制速率或在必要时进行转移来实现适当的放置。
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Simulation of Squeeze Treatment/Tracer Programme Designs
One of the biggest challenges in designing squeeze treatments is ensuring appropriate chemical placement along the completion interval. Generally, the chemical slug is bull-headed; therefore, in long horizontal wells and/or crossflow wells, exposing the chemical to all the completion intervals might be difficult. In this paper we introduce a method to evaluate placement efficiency. If placement is inadequate, some sections of the well will be unprotected, resulting in an undesirable situation: the well may appear to be protected because the inhibitor return concentrations measured at surface are above the threshold, but there is a loss of production due to scale deposition in areas of the well not contacted by chemical. In these circumstances inhibitor placement can be accurately determined by production logging, but this can be prohibitively expensive. An alternative is to use tracers to evaluate the layer flow rate distribution, and therefore quantify chemical placement. The objective of this paper is to determine if a tracer package could be deployed as part of a squeeze treatment in challenging wells, in particular in the overflush stage. If there are zones in the wellbore at different pressures, then producing the tracer back in steps at different rates will result in the tracer return concentration profile having characteristic features that can be interpreted to estimate chemical placement. Two three layer cases with crossflow are considered. In both cases, a tracer package was included in the overflush, and the resulting return profiles showed clearly the desired features. The main advantage of this approach is that there is no significant increase in the operational expense. The only additional expense will be the cost of the specific tracer and the subsequent analysis. It is envisaged that the cost is less than 5% of the total squeeze treatment cost. The results of this novel multi-rate post squeeze production stage following injection of tracer demonstrate the feasibility of including such a tracer package in a squeeze treatment. Data collected may then be used to optimise the design of subsequent treatments, to ensure that appropriate placement is achieved by rate control or by diversion, if necessary.
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