Rajic Ljiljana, Fallahpour Noushin, Alshawabkeh Akram N
Department of Civil and Environmental Engineering, Northeastern University, 400 Snell Engineering, 360 Huntington Avenue, Boston, MA 02115, United States.
Appl Catal B. 2015 Sep 1;174-175:427-434. doi: 10.1016/j.apcatb.2015.03.018.
The electrode sequence in a mixed flow-through electrochemical cell is evaluated to improve the hydrodechlorination (HDC) of trichloroethylene (TCE) in aqueous solutions. In a mixed (undivided) electrochemical cell, oxygen generated at the anode competes with the transformation of target contaminants at the cathode. In this study, we evaluate the effect of placing the anode downstream from the cathode and using multiple electrodes to promote TCE reduction. Experiments with a cathode followed by an anode (C→A) and an anode followed by a cathode (A→C) were conducted using mixed metal oxide (MMO) and iron as electrode materials. The TCE removal rates when the anode is placed downstream of the cathode (C→A) were 54% by MMO→MMO, 64% by MMO→Fe and 87% by Fe→MMO sequence. Removal rates when the anode is placed upstream of the cathode (A→C) were 38% by MMO→MMO, 58% by Fe→MMO and 69% by MMO→Fe sequence. Placing the anode downstream of the cathode positively improves (by 26%) the degradation of aqueous TCE in a mixed flow-through cell as it minimizes the influence of oxygen generated at the MMO anode on TCE reduction at the cathode. Furthermore, placing the MMO anode downstream of the cathode neutralizes pH and redox potential of the treated solution. Higher flow velocity under the C→A setup increases TCE mass flux reduction rate. Using multiple cathodes and an iron foam cathode up stream of the anode increase the removal rate by 1.6 and 2.4 times, respectively. More than 99% of TCE was removed in the presence of Pd catalyst on carbon and as an iron foam coating. Enhanced reaction rates found in this study imply that a mixed flow-through electrochemical cell with multiple cathodes up stream of an anode is an effective method to promote the reduction of TCE in groundwater.
对混合流通式电化学池中电极顺序进行了评估,以改善水溶液中三氯乙烯(TCE)的加氢脱氯(HDC)过程。在混合(未分隔)电化学池中,阳极产生的氧气会与阴极处目标污染物的转化相互竞争。在本研究中,我们评估了将阳极置于阴极下游并使用多个电极来促进TCE还原的效果。使用混合金属氧化物(MMO)和铁作为电极材料,进行了阴极后接阳极(C→A)和阳极后接阴极(A→C)的实验。当阳极置于阴极下游(C→A)时,MMO→MMO序列的TCE去除率为54%,MMO→Fe序列为64%,Fe→MMO序列为87%。当阳极置于阴极上游(A→C)时,MMO→MMO序列的去除率为38%,Fe→MMO序列为58%,MMO→Fe序列为69%。将阳极置于阴极下游可积极改善(提高26%)混合流通式电池中水溶液TCE的降解,因为它能将MMO阳极产生的氧气对阴极处TCE还原的影响降至最低。此外,将MMO阳极置于阴极下游可使处理后溶液的pH值和氧化还原电位中和。C→A设置下更高的流速会提高TCE质量通量降低率。使用多个阴极以及在阳极上游使用泡沫铁阴极分别使去除率提高了1.6倍和2.4倍。在碳载钯催化剂存在下以及作为泡沫铁涂层时,TCE的去除率超过99%。本研究中发现的增强反应速率表明,阳极上游有多个阴极的混合流通式电化学池是促进地下水中TCE还原的有效方法。