重金属废水处理方法综述

水体重金属污染严重影响生态环境与人类健康,需要加以治理。针对重金属废水的不同特点,处理方法也多种多样。本文就各种处理重金属废水的方法进行了简要综述并做了简短展望。     

含油废水处理技术

概述了含油废水的来源、特点、分类及危害,介绍了含油废水的处理方法的原理、优势及存在的问题,同时简述了各种处理方法的最新研究成果,最后提出了含油废水发展趋势。     

冶金高含盐废水处理工艺实践应用

某黄金冶炼厂根据云南当地的实际情况,在废水处理工程中采用太阳能预热-刮板式薄膜蒸法工艺处理黄金深加工过程中产生的高含盐废水,处理效果好,出水稳定,是一种非常有效的处理工艺。氯化物及重金属到达GB5749—2006生活饮用水卫生标准。     

废旧线路板中主要有价金属的生物反应器浸出研究

为探讨可供实际生物浸出应用的反应器规模废旧线路板中有价金属浸出特性和工艺条件,通过设计序批式生物浸出反应器,采用分离到的氧化亚铁硫杆菌Z1作为菌种资源,在考察废旧线路板中有价金属的浸出特性的基础上,确定了反应器运行的最佳工艺条件.结果表明,反应器运行的最佳工艺条件为曝气量1L/min、停留时间30h、搅拌速率300r/min以及粉末投加量12g/L.在此条件下,经过101h可以浸出90.24%的铜.同时,经197h的浸出,可以溶出93.06%的镁、92.00%的锌、85.59%的铝和64.51%的镍.因此,生物浸出反应器能有效回收废旧线路板中的有价金属,为该技术的实际应用提供了实验证据.     

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催化还原法净化处理氮氧化物的工程实例

针对不锈钢产品酸洗处理过程中产生的氮氧化物浓度高、对大气污染的影响大、且难于净化治理等特性,在上海某不锈钢项目中设计了一套酸雾净化系统。该设计解决了酸洗中产生的氮氧化物难以净化的问题,提升了氮氧化物处理技术,它将成为不锈钢酸洗行业中氮氧化物净化处理技术的发展方向。     

Formation pathways of brominated products from benzophenone-4 chlorination in the presence of bromide ions

The brominated products, formed in chlorination treatment of benzophenone-4 in the presence of bromide ions, were identified, and the formation pathways were proposed.Under disinfection conditions, benzophenone-4 would undertake electrophilic substitution generating mono- or di-halogenated products, which would be oxidized to esters and further hydrolyzed to phenol derivatives. The generated catechol intermediate would be transformed into furan-like heterocyclic product. The product species were p H-dependent,while benzophenone-4 elimination was chlorine dose-dependent. When the chlorination treatment was performed on ambient water spiked with benzophenone-4 and bromide ions, most of brominated byproducts could be detected, and the acute toxicity significantly increased as well.     

废弃钻井液不落地达标处理技术在塔里木油田的应用

废弃泥浆中含有化学添加剂、黏土、钻屑、无机盐及含油物质等,pH值较高,一般存放在井场污池内,若管理不善容易造成环境污染。为减少钻井废弃液对环境的污染,针对塔里木油田自身的地理特征和钻井液类型,选取一套经济有效的废弃钻井液无害化处理工艺开展先导试验,解决了废弃钻井液处理施工难度大、工期长、成本高的问题,达到无害化处理的环保效果。     

Arsenic removal from groundwater by acclimated sludge under autohydrogenotrophic conditions

Arsenic in the environment is attracting increasing attention due to its chronic health effects. Although arsenite(As(III)) is generally more mobile and more toxic than arsenate(As(V)), reducing As(V) to As(III) may still be a means for decontamination, because As(III) can be removed from solution by precipitation with sulfide or by adsorption or complexation with other metal sulfides. The performance of As(V) bio-reduction under autohydrogenotrophic conditions was investigated with batch experiments. The results showed that As(V) reduction was a biochemical process while both acclimated sludge and hydrogen were essential. Most of the reduced arsenic remained in a soluble form, although 20% was removed with no addition of sulfate, while 82% was removed when sulfate was reduced to sulfide. The results demonstrated that the reduced arsenic was re-sequestered in the precipitates, probably as arsenic sulfides. Kinetic analysis showed that pseudo first-order kinetics described the bio-reduction process better than pseudo second-order. In particular, the influences of pH and temperature on As(V) reduction by acclimated sludge under autohydrogenotrophic conditions and total soluble As removal were examined. The reduction process was highly sensitive to both pH and temperature, with the optimum ranges of pH 6.5–7.0 and 30–40°C respectively. Furthermore, Arrhenius modeling results for the temperature effect indicated that the As(V) reduction trend was systematic. Total soluble As removal was consistent with the trend of As(V) reduction.     

Nitrogen mass balance in a constructed wetland treating piggery wastewater effluent

The nitrogen changes and the nitrogen mass balance in a free water surface flow constructed wetland （CW） using the four-year monitoring data from 2008 to 2012 were estimated. The CW was composed of six cells in series that include the first settling basin （Cell 1）, aeration pond （Cell 2）, deep marsh （Cell 3）, shallow marsh （Cell 4）, deep marsh （Cell 5） and final settling basin （Cell 6）. Analysis revealed that the NH4＋-N concentration decreased because of ammonification which was then followed by nitrification. The NO4＋-N and NO4＋-N were also further reduced by means of microbial activities and plant uptake during photosynthesis. The average nitrogen concentration at the influent was 37,819 kg/year and approximately 45% of that amount exited the CW in the effluent. The denitrification amounted to 34% of the net nitrogen input, whereas the accretion of sediment was only 7%. The biomass uptake of plants was able to retain only 1% of total nitrogen load. In order to improve the nutrient removal by plant uptake, plant coverage in four cells （i.e., Cells 1, 3, 4 and 5） could be increased.