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Co-precipitation of Radium with Barium and Strontium Sulfate and Its Impact on the Fate of Radium during Treatment of Produced Water from Unconventional Gas Extraction

机译:镭与硫酸锶和锶共沉淀及其在处理非常规抽采采出水过程中对镭命运的影响

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摘要

Radium occurs in flowback and produced waters from hydraulic fracturing for unconventional gas extraction along with high concentrations of barium and strontium and elevated salinity. Radium is often removed from this wastewater by co-precipitation with barium or other alkaline earth metals. The distribution equation for Ra in the precipitate is derived from the equilibrium of the lattice replacement reaction (inclusion) between the Ra~(2+) ion and the carrier ions (e.g., Ba~(2+) and Sr~(2+)) in aqueous and solid phases and is often applied to describe the fete of radium in these systems. Although the theoretical distribution coefficient for Ra-SrSO_4 (K_d = 237) is much larger than that for Ra-BaSO_4 (K_d = 1.54), previous studies have focused on Ra-BaSO_4 equilibrium. This study evaluates the equilibria and kinetics of co-precipitation reactions in Ra-Ba-SO_4 and Ra-Sr-SO_4 binary systems and the Ra-Ba-Sr-SO_4 ternary system under varying ionic strength (IS) conditions that are representative of brines generated during unconventional gas extraction. Results show that radium removal generally follows the theoretical distribution law in binary systems and is enhanced in the Ra-Ba-SO_4 system and restrained in the Ra-Sr-SO_4 system by high IS. However, the experimental distribution coefficient (K_d') varies widely and cannot be accurately described by the distribution equation, which depends on IS, kinetics of carrier precipitation and does not account for radium removal by adsorption. Radium removal in the ternary system is controlled by the co-precipitation of Ra-Ba-SO_4, which is attributed to the rapid BaSO_4 nucleation rate and closer ionic radii of Ra2+ with Ba2t than with Sr~(2+), Carrier (i.e., barite) recycling during water treatment was shown to be effective in enhancing radium removal even after co-precipitation was completed. Calculations based on experimental results show that Ra levels in the precipitate generated in centralized waste treatment facilities far exceed regulatory limits for disposal in municipal sanitary landfills and require careful monitoring of allowed source term loading (ASTL) for technically enhanced naturally occurring materials (TENORM) in these landfills. Several alternatives for sustainable management of TENORM are discussed.
机译:镭出现在水力压裂的返排液和采出水中,用于非常规的瓦斯抽采,以及高浓度的钡和锶和高盐度。通常通过与钡或其他碱土金属共沉淀从该废水中除去镭。沉淀物中Ra的分布方程由Ra〜(2+)离子与载流子离子(例如Ba〜(2+)和Sr〜(2+)之间的晶格置换反应(包含)的平衡得出。 )在水相和固相中,通常用于描述这些系统中镭的含量。尽管Ra-SrSO_4(K_d = 237)的理论分布系数比Ra-BaSO_4(K_d = 1.54)的理论分布系数大得多,但先前的研究集中在Ra-BaSO_4平衡上。这项研究评估了在代表盐水的不同离子强度(IS)条件下,Ra-Ba-SO_4和Ra-Sr-SO_4二元体系和Ra-Ba-Sr-SO_4三元体系中共沉淀反应的平衡和动力学。非常规气体提取过程中产生的。结果表明,镭的去除通常遵循二元体系中的理论分布规律,并且在Ra-Ba-SO_4体系中得到增强,而在Ra-Sr-SO_4体系中则受到高IS的抑制。然而,实验分布系数(K_d')变化很大,不能用分布方程精确地描述,分布方程取决于IS,载流子沉淀的动力学,并且不能解释吸附引起的镭去除。三元体系中的镭去除受Ra-Ba-SO_4的共沉淀控制,这归因于BaSO_4的快速成核速率和Ra2 +与Ba2t的离子半径比与Sr〜(2+),载流子(即,即使在完成共沉淀后,水处理过程中的重晶石回收也能有效提高镭的去除率。根据实验结果进行的计算表明,集中式废物处理设施中产生的沉淀物中的Ra含量远远超过了用于市政卫生垃圾填埋场的管理限制,并且需要仔细监测技术上增强的天然存在物质(TENORM)的允许源负荷(ASTL)。这些垃圾填埋场。讨论了TENORM可持续管理的几种选择。

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  • 来源
    《Environmental Science & Technology》 |2014年第8期|4596-4603|共8页
  • 作者单位

    Department of Civil and Environmental Engineering, University of,National Energy Technology Laboratory (NETL), Pittsburgh, Pennsylvania 15236, United States;

    National Energy Technology Laboratory (NETL), Pittsburgh, Pennsylvania 15236, United States,Department of Civil and Environmental Engineering, Carnegie Mellon University, Pittsburgh, Pennsylvania 15213, United States;

    National Energy Technology Laboratory (NETL), Pittsburgh, Pennsylvania 15236, United States;

    Department of Civil and Environmental Engineering, University of Pittsburgh, Pittsburgh, Pennsylvania 15261, United States,National Energy Technology Laboratory (NETL), Pittsburgh, Pennsylvania 15236, United States;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);美国《化学文摘》(CA);
  • 原文格式 PDF
  • 正文语种 eng
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