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Arsenic Removal from Drinking Waters Containing Varying Alkalinityand Silicate Levels

机译:改变碱度和硅酸盐含量的饮用水中的砷去除

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This research deals with removal of As(V) from waters containing different levels ofrnCa2+, alkalinity, and silicate using ArsenilTM - a nanophase Fe-Mn oxide coated natural zeolitern(U.S. Patent No. 6,790,363). Studies have shown that adsorptive media perform poorly underrnfollowing water chemistries: 1) high pH, 2) high Ca2+ and alkalinity, and 3) high silicate. In highrnCa2+ and alkalinity waters, the primary reason may be due to the CaCO3 formation resulting inrnsurface passivation/fouling and/or site inaccessibility. Lowering the pH of these waters to 7rnimproved the As(V) removal efficiency of the medium, and this may be attributed to thernreduction or elimination of water alkalinity (See Appendix I).rnIn the first part of the study, Dallas, TX municipal water was spiked with As(V) only as itrncontains low Ca2+, alkalinity, and silicate levels. This is representative of As water chemistry inrnNortheast and Midwest regions of USA. The Dallas water spiked with 25 ppm Si along withrnAs(V) simulate water conditions in the Pacific Southwest regions. We maintained the influentrnwater pH at 7 as these waters contain high alkalinity and in the presence of high Ca2+ formsrnCaCO3 in the intra- and inter-particle void spaces resulting in decreased As sorption. Based onrnthermodynamics, the dominant silicate species in the waters with pH ranging from 6 to 8.5 isrnH4SiO40 ( a neutral species), and lowering the pH will not revert significantly to charged silicaternspecies. Since, the pH was decreased to 7 in this study no attempt was made to increase waterrnalkalinity.rnFirst, bench scale studies were conducted followed by pilot-scale studies using As(V)rnspecies, as these are the most dominant oxidation state in US waters. Bench scale studies werernuseful to provide As sorption properties and Empty Bed Contact Time (EBCT) for designing therncolumn studies.rnThe column studies were performed using Dallas, TX municipal water containing pH 8.2,rnlow alkalinity (76 mg CaCO3 per L) and low Ca2+ (40 ppm) and Si (<3 ppm). The influent waterrnspiked with 38 ppb As with EBCT of 5 min, and 115 ppb As with EBCT of 10 min passedrn10,138 and 5,242 bed volumes; respectively. In case of the column studies with influent waterrnmaintained at 25 ppm Si and pH 7, the column with As level of 25 ppb with EBCT of 10 minrnpassed 14,911 bed volumes and the 50 ppb As spiked column with EBCT of 10 min passedrn8,133 bed volumes. In both the columns the effluent As levels were below the detection limits.rnThere was also no significant sorption of Ca2+ and Si by the ArsenilTM medium.
机译:这项研究涉及使用ArsenilTM-纳米相Fe-Mn氧化物涂覆的天然沸石从含有不同水平的Ca2 +,碱度和硅酸盐的水中去除As(V)(美国专利号6,790,363)。研究表明,吸附介质在水化学方面的表现不佳:1)高pH,2)高Ca2 +和碱度以及3)高硅酸盐。在高Ca2 +和碱度的水中,主要原因可能是由于形成CaCO3导致表面钝化/结垢和/或无法进入场地。将这些水的pH值降低至7可以提高介质对As(V)的去除效率,这可能归因于水碱度的降低或消除(请参阅附录I)。rn在研究的第一部分,德克萨斯州达拉斯的市政用水仅当As(V)包含低的Ca2 +,碱度和硅酸盐含量时,才添加As(V)。这是美国东北和中西部地区水化学的代表。达拉斯水掺入25 ppm Si和rnAs(V)可以模拟太平洋西南地区的水况。我们将进水的pH值保持在7,因为这些水含有高碱度,并且在颗粒内和颗粒间空隙中存在高Ca2 +形式的CaCO3,导致As吸附降低。根据热力学,pH范围为6至8.5 isrnH4SiO40(中性物种)的水域中占优势的硅酸盐物质(降低了pH值)不会显着恢复为带电荷的硅盐物种。由于在此研究中pH值降至7,因此未尝试增加水碱度。首先,进行了规模试验,然后使用As(V)物种进行中试规模研究,因为这是美国水域中最主要的氧化态。进行基准规模研究对于设计吸附柱研究提供了As吸附特性和空床接触时间(EBCT).rn色谱柱研究使用的是德克萨斯州达拉斯市的pH值为8.2,碱度较低(76 mg CaCO3 / L)和低Ca2 +( 40 ppm)和Si(<3 ppm)。 EBCT在5 min时进水量为38 ppb As,在10 min EBCT中进水量为115 ppb As,进水量为10,138和5,242床体积。分别。在进水量保持在25 ppm Si和pH 7的进水条件下进行色谱柱研究的情况下,As水平为25 ppb且EBCT为10分钟的色谱柱通过14,911床体积,而50 ppb As掺入的EBCT为10分钟的色谱柱通过了8,133床体积。 。在这两个色谱柱中,废水中的As含量均低于检测极限。ArsenilTM介质也没有明显的Ca2 +和Si吸附。

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