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Performance of ultrafiltration as a pre-concentration stage for the treatment of oxyfluorfen by electrochemical BDD oxidation

机译:通过电化学BDD氧化治疗氧氟荷芬的超滤护性能

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The present work deals with the use of ultrafiltration as a pre-concentration stage in the electrochemical degradation of a non-polar organochlorine compound (oxyfluorfen) with boron-doped diamond (BDD) anodes. The first stage of the work consisted in evaluating the performance of a pilot scale ultrafiltration unit to concentrate a solution of a commercial formulation of oxyfluorfen (Barre (R)) at total recirculation mode. The ultrafiltration membrane exhibited a total rejection of oxyfluorfen, around 70% rejection of TOC and a permeate flux of 285.1 L h(-1) m(-2) at 4 bar and 25 degrees C. The rejection of oxyfluorfen is higher than expected due to the presence of surfactant compounds in the commercial formulation selected, which promotes a mechanism of micellar enhanced ultrafiltration. Next, a discontinuous ultrafiltration test was performed, maintaining this high rejection of oxyfluorfen and observing a limited contribution of fouling mechanisms, according to the adjustment of the data to fouling models. Regarding the electrochemical oxidation of the concentrate with BDD anodes, it was observed an increase in the specific power consumption from 590 kWh kg(-1) for the raw solution to 882 kWh kg(-1) for the concentrate. This unexpected result can be explained due to the limited rejection of the soluble fraction in the ultrafiltration stage, what produced a lower concurrence of oxidants in the electrochemical oxidation step. According to these results, it can be stated that it is worth using ultrafiltration as a concentration stage for commercial formulations of non-polar organochlorines with both high rejection and flux, although it should be combined with degradation technologies different from electrochemical oxidation.
机译:本工作涉及使用超滤作为具有硼掺杂金刚石(BDD)阳极的非极性有机氯化合物(Oxyluorfen)的电化学降解中的预浓度阶段。该工作的第一阶段包括评估试验规模超滤单元的性能,以集中在总再循环模式下浓缩氧氟氟芬(Barre(R))的商业配方的溶液。超滤膜的总抑制氧氟荷芬,约70%的TOC抑制和285.1 L H(-1)m(-2)的渗透通量,在4巴和25℃下抑制氧氟量抑制率高于预期在选择的商业制剂中存在表面活性剂化合物,促进胶束增强的超滤机制。接下来,根据数据调整到污垢模型,执行不连续的超滤试验,保持这种高抑制氧氟荷芬并观察结垢机制的有限贡献。关于浓缩物与BDD阳极的电化学氧化,观察到从590 kWh kg(-1)的浓度为浓缩溶液的590 kwh kg(-1)的特定功耗的增加。由于超滤阶段中可溶性级分的可溶性级分的排斥,可以解释这种意外结果,在电化学氧化步骤中产生的氧化剂的较低同时。根据这些结果,可以说,值得使用超滤作为具有高抑制和助焊剂的非极性有机氯的商业配方的浓度阶段,尽管它应该与不同于电化学氧化不同的降解技术。

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