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Atrazine degradation by in situ electrochemically generated ozone

机译:原位电化学生成臭氧降解去津

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A study on the evaluation of the effectiveness of atrazine degradation by in situ electrochemically generated ozone was conducted. Ti/3-Pb02 electrodes were used as anodes for the ozone.production. The rate of ozone generation, the ozone saturation concentration and the atrazine degradation rate increased with increasing current density. The maximum rate was close to 40 mg h~(-1), the dissolved ozone concentration was 1.6 mg L~(_1) for a current density of 1.5 kA m~(-2) and the electrochemical efficiency was around 6%. The degradation data followed a pseudo first-order kinetic. The values of the rate constants were 6.2 x 10~(-3), 8.8 x 10~(-3),and 1.21 x 10~(-2) min~(-1) for 0.5,1.0, and 1.5 kA m~(-2), respectively. The degradation took place by the combined oxidation with O3 and ~·OH generated at the Ti/β-PbO2 anode surface and by ozone decomposition. The rate was electrochemically controlled up to approximately 90% of degradation and by mass transfer thereafter. The degradation mechanism was comprised mainly by dealkylation followed by a slow dechlorination of the atrazine molecule. Continuous atrazine degradation tests were conducted in a column containing a porous medium with the purpose of determining whether the in situ electrochemical production of the oxidants ~·OH/O3 is effective at reducing the atrazine concentration in the transported flux across the bed. The work demonstrates the potential applicability of the continuous system for in situ atrazine degradation in underground waters, and provides a basis for the future development of this technology.
机译:进行了对原位电化学生成臭氧降解阿特拉津的有效性的评估研究。 Ti / 3-PbO2电极被用作生产臭氧的阳极。臭氧的产生速率,臭氧饱和浓度和the去津降解速率随电流密度的增加而增加。当电流密度为1.5 kA m〜(-2)时,最大溶解速率接近40 mg h〜(-1),溶解的臭氧浓度为1.6 mg L〜(_1),电化学效率约为6%。降解数据遵循伪一级动力学。对于0.5、1.0和1.5 kA m〜,速率常数的值分别为6.2 x 10〜(-3),8.8 x 10〜(-3)和1.21 x 10〜(-2)min〜(-1)。 (-2)。降解是通过在Ti /β-PbO2阳极表面产生的O3和〜·OH的联合氧化以及臭氧的分解而发生的。通过电化学控制该速率,直至降解的大约90%,然后通过传质进行控制。降解机理主要是通过去烷基化,然后将r去津分子缓慢脱氯。在包含多孔介质的柱中进行连续的at去津降解试验,目的是确定氧化剂〜·OH / O3的原位电化学生产是否有效降低了床层输送通量中flux去津的浓度。这项工作证明了连续系统对地下水中原位阿特拉津降解的潜在适用性,并为该技术的未来发展提供了基础。

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