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Adsorptive ozonation of 2-methylisoborneol in natural water with preventing bromate formation

机译:2-甲基异冰片酚在天然水中的吸附性臭氧化反应,可防止溴酸盐的形成

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This paper presents an application of our newly developed adsorptive ozonation process using a high silica zeolite adsorbent (USY) for drinking water treatment. First, the adsorption of 2-methylisoborneol (2-MIB) on USY in a river water/pure water mixture was clarified by a batch-type adsorption experiment. The results showed that 2-MIB was adsorbed on USY; however, almost all of the adsorbed 2-MIB was desorbed over time. The desorption rate was increased with the ratio of river water to pure water, indicating that compounds dissolved in the river water, such as natural organic matter (NOM), prevent the adsorption of 2-MIB on USY. Second, the ability of the river water to consume ozone was confirmed in an experiment using a USY-packed column reactor. The ozone consumption was obviously increased by the presence of USY, indicating that USY-adsorbing compounds dissolved in the river water (probably small size NOM) consumed the ozone. However, the rapid ozone consumption was occurred by 6-8 s in the retention times when 3.14-4.38 mg L~(-1) of water dissolved ozone was fed, this rapid ozone consumption lasted no more than these times. This result revealed that the rapid consumption of ozone by the adsorptive compounds in our process could be avoided within a certain retention time (6-8 s; especially for the river water used in this study) when enough concentration of ozone (3.14 mg L~(-1) or more; same above) was supplied. We therefore performed a trial in which 2-MIB dissolved in river water was continuously decomposed using a USY-packed column with various ozone concentrations. In the process, the adsorptive compound dissolved in the river water adsorbed and reacted with ozone in the parts of the apparatus upstream of the column, while the adsorption and decomposition of 2-MIB took place in the parts of the apparatus downstream of the column. This resulted in a sufficient 2-MIB decomposition with minimizing bromate ion formation.
机译:本文介绍了使用高硅沸石吸附剂(USY)的新开发的吸附臭氧化工艺在饮用水处理中的应用。首先,通过分批式吸附实验弄清了2-甲基异冰片醇(2-MIB)在河水/纯水混合物中在USY上的吸附。结果表明2-MIB吸附在USY上。然而,随着时间的流逝,几乎所有吸附的2-MIB都被解吸。解吸速率随河水与纯水的比例增加而增加,表明溶解在河水中的化合物(例如天然有机物(NOM))阻止了2-MIB在USY上的吸附。其次,使用装有USY的塔式反应器的实验证实了河水消耗臭氧的能力。 USY的存在明显增加了臭氧消耗,表明溶解在河水中的USY吸附化合物(可能是小分子NOM)消耗了臭氧。然而,当加入3.14-4.38 mg L〜(-1)的水溶臭氧时,在保留时间内迅速消耗臭氧的时间为6-8 s,这种快速消耗臭氧的时间不超过这些时间。该结果表明,在足够的臭氧浓度(3.14 mg L〜)下,可以在一定的保留时间内(6-8 s;尤其是本研究中使用的河水)避免吸附剂快速消耗臭氧。 (-1)或更多;与以上相同)。因此,我们进行了一项试验,其中使用具有各种臭氧浓度的USY填充柱对溶于河水中的2-MIB进行连续分解。在此过程中,溶解在河水中的吸附性化合物在塔的上游装置部分与臭氧发生吸附和反应,而2-MIB的吸附和分解则在塔的下游装置部分发生。这导致2-MIB充分分解,同时减少了溴酸根离子的形成。

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