A Novel View of Barium Sulfate Deposition in Stainless Steel Tubing

A. Lu, G. Ruan, K. Harouaka, Dushanee Sriyarathne, Wei Li, Guannan Deng, Yue Zhao, Xing-lei Wang, A. Kan, M. Tomson
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引用次数: 1

Abstract

Deposition of inorganic scale has always been a common problem in oilfield pipes, especially in raising safety risk and producing cost. However, the fundamentals of deposition mechanism and the effect of various surface, temperature, flow rate and inhibitors on deposition rate has not been systematically studied. The objective of this research is to reveal the process of barium sulfate deposition on stainless steel surfaces. In this work a novel continuous flow apparatus has been set up to enable further investigation of deposition rate, crystal size and morphology and the effect of scale inhibitor. In this apparatus supersaturate barium sulfate solution is mixed and passed through a 3 feet stainless steel tubing with ID = 0.04 inch or 0.21 inch at 70 to 120 degree C. The barium concentration is measured at the effluent to quantify the concentration drop. After 1 to 200 hours the tubing is cut into pieces to measure the barite deposition amount and observe the barite crystal morphology using SEM. Under the experimental conditions, the deposition rate along the stainless steel tubing can be modelled by second order crystal growth kinetics, the SEM micrograph also shows that most of deposited barite is micrometer sized crystals. The highest deposition rate happens at the beginning of the tubing even before the expected induction time of bariums sulfate. The results indicated that the deposition happens even before the mixed solution is expected to form particles, which suggest that the heterogeneous nucleation might be the dominate mechanism in the initial stage, then crystal growth takes place and governs the deposition. The mechanism of scale attachment to tubing surface has never been well-understood. The apparatus in this work provides a reliable and reproducible method to investigate barium sulfate deposition. The findings in this research will enhance our knowledge of mineral scale deposition process, and aid the use of inhibitors in mineral scale control.
不锈钢管中硫酸钡沉积的新观点
无机水垢的沉积一直是油田管道生产中普遍存在的问题,尤其会增加管道的安全风险和生产成本。然而,沉积机理的基本原理以及不同表面、温度、流速和抑制剂对沉积速率的影响尚未得到系统的研究。本研究的目的是揭示硫酸钡在不锈钢表面沉积的过程。本文建立了一种新型的连续流动装置,以进一步研究沉积速率、晶体尺寸和形态以及阻垢剂的效果。在该装置中,过饱和硫酸钡溶液混合并在70至120摄氏度下通过直径为0.04英寸或0.21英寸的3英尺不锈钢管。在流出处测量钡浓度以量化浓度下降。1 ~ 200小时后,将管材切成片,测量重晶石沉积量,用扫描电镜观察重晶石晶体形貌。在实验条件下,沿不锈钢管的沉积速率可以用二级晶体生长动力学来模拟,SEM显微图也表明,沉积的重晶石大部分是微米级的晶体。最高沉积速率发生在管道的开始,甚至在预期的硫酸钡诱导时间之前。结果表明,在混合溶液形成颗粒之前,沉积就已经发生了,这表明在初始阶段,非均相成核可能是主要的机制,然后发生晶体生长并控制沉积。结垢在油管表面的附着机理一直没有得到很好的理解。本装置为研究硫酸钡沉积提供了一种可靠、重复性好的方法。本研究结果将增强我们对矿物结垢过程的认识,并有助于抑制剂在矿物结垢控制中的应用。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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