超滤工艺净化微污染原水的试验研究

采用混凝沉淀-超滤工艺对微污染原水进行试验,对组合工艺的除污染特性进行了研究。结果表明,组合工艺对浊度、颗粒物和藻类的去除效果非常好。出水浊度稳定在0.1NTU以下,水中粒径>2μm的颗粒数约19个/mL,藻类平均数量约为2.2×104个/L。在去除有机物方面,组合工艺对高锰酸盐指数、UV254和DOC的去除率分别为38.0%、15.2%和32.6%,其中对高锰酸盐指数的去除效果较为突出,出水高锰酸盐指数浓度为2.69~2.87mg/L。组合工艺去除的有机物是分子量大于3KD的大分子有机物,对小分子有机物去除效果不明显。其中,混凝沉淀主要去除了水中的疏水性有机物和亲水荷电有机物,超滤膜去除的有机物则以亲水中性有机物为主。在工艺运行期间,超滤膜的跨膜压差增加了约12.3%,跨膜压差的升高主要由被超滤膜吸附的小分子有机物产生。     

MIEX预处理技术对长江原水中有机物的去除效能

利用烧杯试验研究了磁性离子交换树脂（magnetic ion exchange resin,MIEX）预处理对长江原水中有机物的去除效能,以总溶解有机碳(DOC)、254 nm紫外吸收值(UV254)、有机物相对分子质量分布、有机物分级、紫外扫描以及消毒副产物生成量等指标进行表征.结果表明,长江水源水中的有机物主要为小分子亲水性有机物,其含量占有机物总量的50%以上;MIEX预处理可以有效降低水中有机物的含量,投加量为10 mL/L、接触时间为15 min时,DOC的去除率超过35%,相对分子质量和分级的测定结果表明,小分子亲水性部分有机物的去除导致了DOC去除效果的改善;从紫外扫描结果可看出,MIEX预处理对在190～250 nm波长时有强吸收的有机物去除效果非常明显,但对在高于250 nm波长处有吸收的有机物去除效果与混凝阶段的效果相近.     

挥发及半挥发有机物污染场地蒸汽抽提修复技术原理与影响因素

土壤蒸汽抽提技术(soil vapor extraction,SVE)因其对挥发性/半挥发性有机物污染土壤治理的有效性、经济性和环境友好性,被广泛用于该类有机物污染土壤的修复.本文介绍了SVE技术的基本原理和工程技术实施的基本步骤,并且讨论了影响SVE修复技术的因素和3种SVE强化技术,最后概述了我国对SVE技术的研究...     

Pollutant removal from municipal wastewater employing baffled subsurface flow and integrated surface flow-floating treatment wetlands

This article reports pollutant removal performances of baffled subsurface flow, and integrated surface flow-floating treatment wetland units, when arranged in series for the treatment of municipal wastewater in Bangladesh. The wetland units （of the hybrid system） included organic, inorganic media, and were planted with nineteen types of macrophytes. The wetland train was operated under hydraulic loading fluctuation and seasonal variation. The performance analyses （across the wetland units） illustrated simultaneous denitrification and organics removal rates in the first stage vertical flow wetland, due to organic carbon leaching from the employed organic media. Higher mean organics removal rates （656.0 g COD]（m2.day）） did not completely inhibit nitrification in the first stage vertical flow system; such pattern could be linked to effective utilization of the trapped oxygen, as the flow was directed throughout the media by the baffle walls. Second stage horizontal flow wetland showed enhanced biodegradable organics removal, which depleted organic carbon availability for denitrification. The final stage integrated wetland system allowed further nitrogen removal from wastewater, via nutrient uptake by plant roots （along with nitrification）, and generation of organic carbon （by the dead macrophytes） to support denitrification. The system achieved higher E. coli mortality through protozoa predation, E. coli oxidation, and destruction by UV radiation. In general, enhanced pollutant removal efflciencies as demonstrated by the structurally modified hybrid wetland system signify the necessity of such modification, when operated under adverse conditions such as： substantial input organics loading, hydraulic loading fluctuation, and seasonal variation.     

处理难降解有机物的新型SBR反应器的发展

本文在分析ＳＢＲ 工艺特点的基础上,从反应器本身及ＳＢＲ 反应运行工序的设计两方面对处理难降解有机物新型ＳＢＲ 反应器的发展作了论述。分析认为ＳＢＲ 工艺将在中小型企业含难降解有机物工业废水处理中广泛应用。     

ABA对米槠和格氏栲种子发育的影响

采用酶联免疫分析法（ＥＬＩＳＡ） 提取和测定米槠和格氏栲发育过程中果实内ＡＢＡ含量,并用不同浓度ＡＢＡ喂养,测定果实不同发育期对外源ＡＢＡ的敏感性．用放射性同位素法测定ＡＢＡ对贮藏蛋白质的积累作用,结果表明：在米槠和格氏栲种子发育过程中内源ＡＢＡ 含量逐渐上升,两者均在１０ 月５ 日达到峰值,米槠为１６４８ ｎｇｇ,格氏栲为１ ４６８ ｎｇｇ,随后ＡＢＡ含量均逐渐下降．果实成熟采收时,ｃ（ＡＢＡ） 仅为高峰时的１９．随着果实的发育对外加ＡＢＡ的敏感性逐渐变小,ｃ（ＡＢＡ）＝１０－４ ｍｏｌＬ－１ 可以完全抑制１０ 月２５ 日（ 米槠） 和１０ 月１５ 日（ 格氏栲） 前种子发芽,但对完全成熟的种子ｃ（ＡＢＡ）＝１０－２ ｍｏｌＬ－１ 亦不能抑制发芽．ＡＢＡ 对成熟前期胚的贮藏蛋白质合成无影响,但能促进成熟中后期胚的贮藏蛋白质的积累作用,ＡＢＡ维持米槠和格氏栲贮藏蛋白质合成和积累作用表现在转录水平上．     

人工湿地废水处理机理

对人工湿地的构造、作用机理进行了较详尽的说明,湿地中物理、化学及生物协同作用以及湿地植物输氧造成的湿地基质中好氧、缺氧和厌氧状态的交替出现是保证其对氮磷及有机物具有较强处理效率的原因。研究表明：对进水浓度较低的城市污水,湿地的ＢＯＤ５和ＣＯＤ去除率大于８０％,出水ＢＯＤ２为１０ｍｇ／Ｌ左右。总氮及总磷去除率可大６０％和９０％,较常规二级处理方式具有一定的优越性。     

焦化废水中难降解有机物去除的研究

研究了以UV(紫外线)照射、O₃氧化及厌氧酸化作为预处理方法来提高焦化废水生物降解性能的可行性和作用机理,并由此提出了一条新的工艺路线:A-A/O工艺。研究表明,以A-A/O工艺去除焦化废水中的难降解有机物效果显著,经济可行。      

Modification on the conventional procedure to measure AOC in drinking water

Additional phosphorus will be introduced to water sample if the conventional procedure is used to measure assimilable organic carbon(AOC) in drinking water. It has been shown that there are the cases that phosphorus is the limiting nutrient for microbial growth in drinking water. The measured value of AOC would not be able to indicate appropriately the regrowth potential of bacteria in this case. The conventional procedure used to measure AOC was modified to avoid the introduction of additional phosphorus to water sample in this study. It was shown that it was feasible to measure AOC in water using the modified procedure. Furthermore, the measured value of AOC determined by the modified procedure could indicate appropriately the regrowth potential of bacteria in drinking water despite either organics or phosphorus was the limiting nutrient for bacterial regrowth.