Co(II)配合物的合成、结构表征及对有毒有机化合物的催化还原研究硝基苯酚和硝基苯胺

A. Saleh, A. Faheim, Omayma Mostafa, Z. Abdelwahab, Aida A. Salman
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摘要

电解(ED)是一种利用位于电场中的膜分离污染物的现代技术,因此已被用于工业废水处理。ED电池的基石是一堆膜,其平面板由阳离子(CM)和阴离子(AM)选择性膜组成。为了研究限制电流密度(LCD)、电流效率和膜电阻等设计要求,采用实验室实验规模,采用不锈钢316电极[阴极(-)和阳极(+)],pH值为6.8,低压电源能量为24.8 V,从盐溶液中去除每种金属(铁、锰、镍、铜、锌、铅和镉)离子约100mg/L。改进后的膜和电极提高了其耐久性和电导率,浓缩物和产物的循环流量分别为90和34 L/hr,分别为25和9.4 ml/s,连续运行的能耗为7 ~ 11 kWh/ m3。用于工业废水;实验结果表明,在4小时的处理时间内,活性炭的去除率达到了91.87%。对重金属离子的去除率分别为1.521、0.96、0.123、1.41、0.94、0.12和0.097 mg/L,通过ED电池后的去除率分别为0.23、0.11、0.01、0.22、0.14、0.02和0.014,对重金属离子的去除率分别为84.88、88.54、91.87、84.40、85.11、83.33和85.57%。下一个是长期操作系统的大规模行动。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Synthesis, structural characterization, and catalytic reduction study of Co(II) complex towards toxic organic compounds; nitrophenol, and nitroaniline
Electrolysis (ED) is a modern technology for separating pollutants using membranes located in an electric field and has therefore been used in industrial wastewater treatment. The cornerstone of an ED cell is a stack of membranes whose planar plate is composed of cation (CM) and anion (AM) selective membranes. To investigate design requirements such as limiting current density (LCD), current efficiency and membrane resistance by laboratory experimental scale using an ED cell with electrodes, stainless steel 316 [cathode (-) and anode (+)],value of pH equal 6.8 and low voltage supply energy of 24.8 V is installed to remove about 100mg/L for each metal (Iron, Manganese, Nickel, Copper, Zinc, Lead, and Cadmium) ions out of solution of salts. The modified membranes and electrodes to upgrade its durability and conductivity, the recycle flow was 90 and 34 L/hr for concentrate and product, respectively, which are 25 and 9.4 ml/s and with consumed 7 to 11 kWh/m 3 for a continuous operation. For industrial wastewater; the results are obtained a best and encouraging specific with removal efficiency (up to 91.87%) during the 4 hr operating time. The result of removing heavy metal ions was 1.521, 0.96, 0.123, 1.41, 0.94, 0.12 and 0.097 mg/L as initial concentrated and after passing through ED cell became finial concentration 0.23, 0.11, 0.01, 0.22, 0.14, 0.02 and 0.014 with removal efficiency 84.88, 88.54, 91.87, 84.40, 85.11, 83.33 and 85.57% for heavy metal ions under study respectively. The next is being acted on large scale for long operating system.
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