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71.
银在活性炭上的吸附行为和机理的研究 总被引:5,自引:0,他引:5
本文研究了银在活性炭上的吸附行为,探讨了影响吸附效率的各种因素。考察了多种溶液对吸附银的洗脱效果,发现银在活性炭上的吸附不是还原吸附,而是以离子形成与活性炭表面的-NH2和=NH形成络合物而被吸附。 相似文献
72.
杨梅 《城市环境与城市生态》2002,15(3):43-44
采用铁屑内电解-絮凝沉淀-气浮分离作预处理,再经生化、后处理等工艺处理酸析糖精废水是经济、高效可行的,出水各项指标可达国家排放标准要求。 相似文献
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74.
The Hg0 vapor adsorption experimental results on a novel sorbent obtained by impregnating a commercially available activated
carbon (Darco G60 from BDH) with silver nitrate were reported. The study was performed by using a fundamental approach, in an
apparatus at laboratory scale in which a synthetic flue gas, formed by Hg0 vapors in a nitrogen gas stream, at a given temperature
and mercury concentration, was flowed through a fixed bed of adsorbent material. Breakthrough curves and adsorption isotherms were
obtained for bed temperatures of 90, 120 and 150°C and for Hg0 concentrations in the gas varying in the range of 0.8–5.0 mg/m3. The
experimental gas-solid equilibrium data were used to evaluate the Langmuir parameters and the heat of adsorption. The experimental
results showed that silver impregnated carbon was very effective to capture elemental mercury and the amount of mercury adsorbed by
the carbon decreased as the bed temperature increased. In addition, to evaluate the possibility of adsorbent recovery, desorption was
also studied. Desorption runs showed that both the adsorbing material and the mercury could be easily recovered, since at the end of
desorption the residue on solid was almost negligible. The material balance on mercury and the constitutive equations of the adsorption
phenomenon were integrated, leading to the evaluation of only one kinetic parameter which fits well both the experimentally determined
breakthrough and desorption curves. 相似文献
75.
Manuela Anzano Alessandra Tosti Marina Lasagni Alfredo Campiglio Demetrio Pite Elena Collina 《环境科学学报(英文版)》2011,23(9):1570-1577
The aim of the research was to develop new products and processes from a manufacturing waste from an Italian metallurgic company. The company produced thin silver metallic films and the production scraps were silver flakes. The possibility to use the silver flakes in water disinfection processes was studied. The antimicrobial activity of the flakes was investigated in batch using Escherichia coli as Gram-negative microorganism model. The flakes did not show any antimicrobial activity, so they were activated with two different processes: thermal activation in reducing atmosphere and chemical activation, obtaining, respectively, reduced flakes (RF) and chemical flakes (CF). The flakes, activated with either treatment, showed antimicrobial activity against E. coli. The kill rate was dependent on the type of activated flakes. The chemical flakes were more efficient than reduced flakes. The kill rate determined for 1 g of CF, 1.0 ± 0.2 min−1, was greater than the kill rate determined for 1 g of RF, 0.069 ± 0.004 min−1. This was confirmed also by the minimum inhibitory concentration values. It was demonstrated that the antimicrobial capability was dependent on flakes amount and on the type of aqueous medium. Furthermore, the flakes maintained their properties also when used a second time. Finally, the antimicrobial activities of flakes were tested in an effluent of a wastewater treatment plant where a variety of heterotrophic bacteria were present. 相似文献
76.
77.
文章采用铁屑一活性炭内电解法作为光合细菌生化处理染料废水的预处理方法,考查了3个主要影响因素(铁炭比、停留时间、初始pH值)。结果表明,最佳的处理条件为:铁炭比为7:3,pH值为5,停留时间为60min。在上述最佳处理条件下,对初始COD为6790mg/L的染料废水处理效率可以达到66.1%,并且废水经预处理后可生化性得到大大提高,有利于后续生化处理的进行。 相似文献
78.
79.
为解决电化学法处理高盐染料废水存在的能耗大、成本高等问题,分别采用溶胶-凝胶法和辊压法制备Ti/SnO_2-Sb阳极和空气阴极,构建了Ti/SnO_2-Sb阳极-空气阴极双极体系(TSSA-ADC)。甲基橙(MO)作为高盐染料废水的典型污染物,考察了电流强度、MO浓度、电解液浓度和初始p H对TSSA-ADC体系和TSSA单阳极体系降解MO的影响。结果表明:与TSSA单阳极体系相比,TSSA-ADC体系具有更好的抗有机负荷冲击、抗盐分冲击、抗酸碱波动能力,能够维护酸碱平衡防止硬度离子结垢。最佳反应条件为电流强度为0.030 A,电解液浓度为3%,MO浓度为100 mg/L,初始pH=6。以MO去除率达到98%为基准,TSSA-ADC体系比TSSA体系可节能74.26%。 相似文献
80.
铁炭微电解工艺处理采油废水的研究 总被引:1,自引:1,他引:1
随着采油废水产生量的逐渐增大以及排放标准的日益严格,寻找一种经济、高效的处理方法显得十分必要。采用铁炭微电解技术对冀东油田采油废水进行了处理。考察了铁屑粒径、pH值、Fe/C质量比和反应时间对COD去除率的影响并设计了正交实验,结果表明,影响微电解工艺的因素主次关系为:pH>Fe/C质量比>反应时间,在最佳条件pH=5,Fe/C质量比为7∶1,反应时间50 min下,原水COD由170 mg/L降至95.6 mg/L,去除率达43.85%,出水满足国家二级排放标准。 相似文献