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首页> 外文期刊>Journal of Chemical Engineering of Japan >UV-Bubble Column Reactor (UV-BCR) for Photolytic Removal of Tetrachloroethylene (PCE) from the Vapor Phase: Methodological Approach
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UV-Bubble Column Reactor (UV-BCR) for Photolytic Removal of Tetrachloroethylene (PCE) from the Vapor Phase: Methodological Approach

机译:用于从气相中光解四氯乙烯(PCE)的紫外气泡塔反应器(UV-BCR):方法学方法

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摘要

Chlorinated volatile organic compounds (CVOCs) such as tri-and tetrachloroethylene (TCE and PCE) are common contaminants of ground watera nd soil. Numerous studies have been carried out with the long-term objective of the development of efficient, destructive on-site technologies for their removal. The so-called advanced oxidation processes (AOPs) were applied in the liquid and in the gas, but were shown to have limited application. In the liquid phase the efficiency was limited due to the presence of OH radical scavengers and UV light absorbers; and in the gas phase due to the production of stable intermediates. A newphotochemical reactor system is described, in which the polluted air (from the air stripper or SVE unit) is absorbed into a bubble column reactor equipped with the UV light (UV-BCR) containing only distilled water and H_2O_2 as a reacting medium. The experiments showed that the oxidation of model pollutan PCE in a liquid phase occurred approximately 6 times faster in an OH radical scavenger-free environment compared to the experiments in which the OH radical scavenger concentration was adjusted to a level usually found in ground waters. It was also observed, that for the certain PCE concentration, there exists an optimal hydrogen peroxide cocentration above and below whic the rate is reduced and could be predicted by the kinetic model under operational conditions of this work. For the experiemnts in which PCE gas was absorbed into the UV-BCR, the influences of the two critical parameters, gas flow rate and the hydrogen peroxide cocentration, were investigated of the two critical parameters, gas flow rate and the hydrogen peroxide concentration, were investigated using the Experimental design methodology. There has been observational evidence of the efficiency of the process (cca 75%-80% PCE gas removal effciency in one flow through the UV-BCR) but the operational parameters still need to be optimized.
机译:氯化挥发性有机化合物(CVOC),例如三氯乙烯和四氯乙烯(TCE和PCE)是地下水和土壤的常见污染物。为了开发有效的,破坏性的现场清除技术,已经进行了许多长期研究。在液体和气体中应用了所谓的高级氧化工艺(AOP),但显示出其应用受限。在液相中,由于存在OH自由基清除剂和紫外线吸收剂,效率受到限制。并且由于产生了稳定的中间体而处于气相中。描述了一种新的光化学反应器系统,其中被污染的空气(来自空气汽提器或SVE单元)被吸收到装有仅包含蒸馏水和H_2O_2作为反应介质的UV光(UV-BCR)的鼓泡塔反应器中。实验表明,与将OH自由基清除剂的浓度调节至通常在地下水中发现的水平相比,在无OH自由基清除剂的环境中,模型花粉聚糖PCE在液相中的氧化速度大约快6倍。还观察到,对于一定的PCE浓度,存在高于和低于该浓度的最佳过氧化氢浓度,速率降低并且可以通过在该工作的操作条件下的动力学模型来预测。对于PCE气体被UV-BCR吸收的实验,研究了气体流速和过氧化氢浓度这两个关键参数对气体流速和过氧化氢浓度的影响。使用实验设计方法进行了调查。有观察到的证据表明该方法的效率(通过UV-BCR的单流中大约75%-80%的PCE气体去除效率),但仍需要优化操作参数。

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