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Sulfate Removal for Barium Sulfate Scale Mitigation -- Kinetic vs. ThermodynamicControls in Mildly Oversaturated Conditions

机译:去除硫酸钡以减轻硫酸钡垢-在轻度过饱和条件下的动力学与热力学控制

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Conventionally, scale mitigation is achieved using chemicalinhibitors either by squeeze treatment into the reservoir orcontinuous injection. However, with new fields encounteringincreasingly more challenging environments, or when theeconomic impact of chemical intervention by squeezetreatment is large (e.g. subsea fields with poor bullheadchemical placement), other methods of scale control such asthe use of low sulphate sea water (LSSW), must be consideredduring the front end engineering and design (FEED) stage of afield development. Nevertheless, for conventional sulphatereduction packages (SRP's) that reduce the sulphateconcentration in the injected sea water typically towards 40 –50 ppm, there remains a residual scaling risk and therequirement for periodic squeeze treatments.Previous work reported at the 2004 SPE OilfieldScale symposium (SPE 87465) examined the level of sulphatereduction required to mitigate the requirement for evenperiodic squeeze treatments against barium sulphate scale.This showed that sulphate levels of 20 ppm were required inorder to prevent scale formation under down hole productionconditions, although it was also demonstrated thatthermodynamically the system remained oversaturated withbarium sulphate.This paper expands considerably on this preliminary"field specific" case and examines the impact of LSSW on thescaling kinetics across a broad range of formation watercompositions (barium ranging from 150 ppm to 650 ppm) andat temperatures between 80oC and 120oC. The papertherefore investigates the relationship between scaling kineticsand thermodynamics in relatively mild scaling environmentsand illustrates that whereas extremely low levels of sulphatewould be required to completely prevent scale from athermodynamic viewpoint, the kinetics of scale formation mayprevent scale precipitation under down hole productionconditions, with additional continuous injection inhibitorapplied at wellheads to protect flow lines etc. In summary,this paper presents results from an extensive series of longterm dynamic flow and pseudo static performance testsdesigned to determine the relative impact of thermodynamicsand kinetics on the residual barium sulphate scaling risksassociated with the injection of LSSW for pressure support.
机译:按照惯例,使用化学药品可减轻水垢 通过挤压处理剂进入油藏或 连续注射。但是,随着新领域的发展 越来越具有挑战性的环境,或者当 挤压化学干预的经济影响 治疗范围较大(例如海底油田,头顶状况不佳) 化学品放置),其他规模控制方法,例如 必须考虑使用低硫酸盐海水(LSSW) 在前端工程和设计(FEED)阶段 现场开发。尽管如此,对于常规硫酸盐 减少硫酸盐的还原包(SRP) 注入海水中的浓度通常接近40 – 50 ppm,仍然存在残留的结垢风险,并且 定期挤压处理的要求。 2004 SPE油田报道的先前工作 规模研讨会(SPE 87465)检查了硫酸盐的水平 减少所需的减少量以达到均匀的要求 定期针对硫酸钡水垢进行挤压处理。 这表明硫酸盐含量要求为20 ppm。 为了防止井下生产中结垢 条件,尽管也证明了 在热力学上,系统保持过饱和 硫酸钡。 本文在此初步内容上做了很大的扩展 “特定于领域”的案例,并研究了LSSW对 广泛的地层水结垢动力学 成分(钡含量范围从150 ppm至650 ppm)和 温度在80oC至120oC之间。论文 因此研究了结垢动力学之间的关系 相对温和的缩放环境中的热力学和热力学 并说明硫酸盐含量极低 将需要完全防止水垢从 从热力学观点看,水垢形成的动力学可能 防止井下生产中结垢 条件下,与其他连续注射抑制剂一起使用 应用于井口以保护流线等。总而言之, 本文介绍了一系列长期的结果 术语动态流和伪静态性能测试 用于确定热力学的相对影响 和动力学对残余硫酸钡结垢风险的影响 与用于压力支持的LSSW注射相关。

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