天然气水合物有效抑制剂的选择方法

A. Kunakova, F. G. Usmanova, I. Vorozhtsova, Iuliia Vladislavovna Lanchuk
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引用次数: 0

摘要

Orenburg油气凝析油田东段气举井的油气生产复杂,包括油管中天然气水合物的形成、关闭阀和控制阀以及气举系统。为了防止水合物的形成,使用了连续供应的甲醇,造成了额外的经济成本和环境风险。因此,寻找新的更有效的试剂来去除和防止天然气水合物的形成非常重要。这项工作的目的是为ESOOGCF条件下选择最有效的水合物形成抑制剂。对天然气水合物形成的热力学和动力学抑制剂进行了研究。由于抑制剂的作用机制不同,对其有效性的评价方法也不同。实验条件尽可能接近现场:采用气液混合模型,确定合适的温度和压力条件。降低水合物形成温度的热力学抑制剂在连续搅拌的GHA 350高压灭菌器中保持恒定温度:温度T=2°C,初始压力50 atm。在12小时内。采用多热法,在8°C ~ - 15°C的温度范围内,采用RCS6设备,初始压力为30 bar,研究了由于吸附在水合物晶体上而减缓水合物形成过程的动力学抑制剂。通过水合物形成气体的初始吸收温度来评价抑制剂的有效性。系统的压降证明了这一点。在研究热力学抑制剂的过程中,还可以直观地记录体系中水合物的形成过程。实验结果发现,热力学抑制剂在产出水中ESOOGCF体积浓度为15%或20%的条件下,可以更好地防止水合物的形成,因为几乎所有研究的试剂都表现出高效率。在动力学抑制剂中,只有两种试剂在体积浓度为产出水量的2.5%和5%时对水合物形成的减少有积极的效果。所有试剂成功通过实验室测试的制造商都被邀请参加现场测试。今天对两种不同类型作用的试剂进行了现场试验。在这些测试中,确定了热力学抑制剂的最低有效浓度- 164 L/天。相比之下,现场试验前的甲醇消耗量为500 L/天,尽管该试剂在技术方面并不逊色于他。根据现场试验结果,水合物形成动力学抑制剂的最小有效用量为50 L/d。因此,在相同的基础试剂技术参数下,应用热力学和动力学的水合物抑制剂具有经济效益。每个单独对象的条件需要一个单独的抑制剂选择,可以显示在这些条件下的最佳效率。目前,水合物抑制剂的有效剂量是在现场试验中确定的,这导致了较高的经济成本和技术风险。本文提出了在实验室中对抑制剂的有效性进行评估,从而降低了试剂选择的成本并最大限度地降低了技术风险。本文介绍了在碱性试剂甲醇前使用低剂量抑制剂的经济效益。本文重点介绍了选择有效水合物形成抑制剂的不同方法。研究对象为奥伦堡凝析油气田东段条件下的水合物形成抑制剂。现在,为了防止水合物的形成,采用了连续供应甲醇的方法。由于需要更有效和更具成本效益的解决方案,人们正在寻找减少水合物形成的新方法。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Approaches to the Selection of Effective Inhibitors of Gas Hydrate Formation
Hydrocarbons production in gas-lift wells of the Eastern section of the Orenburg oil and gas condensate field (ESOOGCF) is complicated by gas hydrates formation in oilwell tubing, shutoff-opening and control valves and gas lift system. In order to prevent hydrate formation, continuous supply of methanol is used, causing additional economic costs and environmental risks. Therefore, it is important to search for new more effective reagents to remove and prevent gas hydrate formation. The aim of this work was to choose the most effective inhibitors of hydrate formation for ESOOGCF conditions. The study was carried out among thermodynamic and kinetic inhibitors for gas hydrates formation. Due to different mechanism of inhibitors action, various approaches were used to evaluate their effectiveness. Experimental conditions were as close as possible to the field ones: the model gas-liquid mixture was used, the appropriate temperature and pressure conditions were determined. Thermodynamic inhibitors which reduce hydrate formation temperature were kept at a constant temperature in the GHA 350 autoclave under continuous stirring: temperature T=2°C and initial pressure 50 atm. during 12 hours. The study of kinetic inhibitors that slow down the process of hydrate formation due to adsorption on hydrate crystals was carried out by polythermic method in the temperature range from 8°C to −15°C using the RCS6 equipment with initial pressure 30 bar. The effectiveness of inhibitors was evaluated by initial temperature of absorption of hydrate-forming gas due to hydrate formation. It was proved by pressure drop in the system. In the process of studying of thermodynamic inhibitors, the formation of hydrates in the system could also be recorded visually. As a result of the experiments it was found that thermodynamic inhibitors better prevent hydrate formation in the conditions of ESOOGCF at concentrations of 15% or 20% by volume in produced water as almost all of the reagents studied showed high efficiency. Among kinetic inhibitors, only two reagents showed positive results in hydrate formation reduce at volume concentrations of 2.5% and 5% of the amount of produced water. All manufacturers whose reagents successfully passed laboratory tests were invited to participate in field tests. For today field tests of two reagents of different types of action have been carried out. During these tests the minimum effective concentration of a thermodynamic inhibitor was determined - 164 L/day. For comparison, methanol consumption before the field tests was 500 L/day despite the fact that the reagent is not inferior to him in technical terms. The minimum effective dosage of the kinetic inhibitor of hydrate formation according to the results of field tests was 50 L/day. Thus, the application of thermodynamic and kinetic inhibitors of hydrate formation is economically profitable under the same technical parameters of the base reagent. The conditions of each individual object require an individual inhibitors selection which can show the best efficiency in these conditions. Currently, effective dosages of hydrate inhibitors are determined during field tests, which lead to high economic costs and technological risks. This paper proposes an assessment of inhibitors' effectiveness in laboratory, which reduces the cost of reagents selection and minimizes technological risks. The paper presents economic benefits of using low-dose inhibitors in front of the basic reagent - methanol. This article focuses on different approaches to the selection of effective inhibitors of hydrate formation. Research objects are hydrate-formation inhibitors for conditions of the Eastern section of the Orenburg oil and gas condensate field. Nowadays continuous supply of methanol is used to prevent hydrate formation. Due to the need for more efficient and cost-effective solutions, searches are being conducted for new ways to reduce hydrate formation.
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