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首页> 外文期刊>Environmental Progress & Sustainable Energy >Treatment of Dyehouse Effluents Using Sequential Combinations of Electrochemical Oxidation, Membrane Separation, and Activated Sludge
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Treatment of Dyehouse Effluents Using Sequential Combinations of Electrochemical Oxidation, Membrane Separation, and Activated Sludge

机译:使用序贯治疗染坊废水电化学氧化的组合,膜分离,活性污泥

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摘要

Reducing water demand in textile sector is one of the important environmental concerns. In this study, individual and combined effects of selected operational parameters on a full-scale electrochemical oxidation (ECO) process treating dyehouse effluent were investigated experimentally. Combinations of variables including current density, wastewater pH, and conductivity resulting in maximum color removal efficiency were determined using the Box-Behnken design method. In addition to color removal, variations in wastewater organic composition before and after ECO were also examined critically. Removal and/or generation of 22 polycyclic aromatic hydrocarbons (PAHs) before and after ECO were investigated under variable operational conditions. Treatability of ECO effluent using conventional activated sludge process was investigated by both full-scale monitoring studies and batch-scale nitrification tests. Toxicity impact of raw, ozonized, and electrochemically treated wastewaters on nitrifiers were also determined and compared. Water reuse and salt recovery alternatives were assessed by full-scale tests in a pilot plant which is composed of nanofiltration (NF), reverse osmosis (RO), and activated sludge processes. Advantages and disadvantages of applying ECO process as a pretreatment prior to membrane-based or biological methods were critically evaluated. The average flux values of NF and RO membranes without ECO were 39 ± 2 and 19.5 ± 1 Lm~(-2) h~(-1), respectively. The average flux values ofNF and RO membranes without ECO were 39 ± 2 and 19.5 ±11 m~(-2) h~(-1), respectively. The permeability of the membranes for raw dyehouse effluent (without ECO) were estimated to be 6.0 ±11 and 0.73 ± 0.6L m~(-2) h~(-1) bar~(-1) Another important observation was formation of some PAHs including naphthalene, acenaphtylene, anthracene, ben-zo(a)anthracene, and benzo(g,h,i)perylene as a function of operational conditions maintained in ECO process.
机译:降低水在纺织行业是一个需求重要的环境问题。研究中,个别和合并的影响选择操作参数全面电化学氧化(ECO)治疗过程染坊废水研究实验。包括电流密度、废水的pH值,电导率导致最大颜色去除使用Box-Behnken效率测定设计方法。废水有机成分的变化之前和之后的生态也检查了批判性的。多环芳烃(多环芳烃)之前和生态进行调查后变量操作条件。使用传统的活性污泥废水过程的全面调查监测研究和batch-scale硝化测试。在电化学处理废水硝化细菌也决定和比较。水重用和盐复苏的替代品在一个试验工厂的全面评估测试这是由纳滤(NF)、反向渗透(RO)和活性污泥过程。应用生态的优点和缺点作为一个前预处理膜基过程或生物方法进行批判性的评估。NF和RO膜的平均变化值没有生态39±2和19.5±1 Lm ~ (2)分别h ~(1)。ofNF和RO膜没有ECO 39±219.5±11 m ~ (2) h ~(1),分别。渗透膜的原始染坊废水(不环保)估计为6.0±11和0.73±0.6 l m ~ (2) h ~(1)酒吧~ (1)另一个重要的观察是形成一些多环芳烃包括萘、acenaphtylene蒽蒽,ben-zo (),苯并苝醌类化合物(g、h、i)作为操作的函数条件维持生态过程。

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