Mobile passive samplers: concept for a novel mode of exposure

Integrative passive sampling with devices such as semipermeable membrane devices generally relies on rigs for month-long static exposures in water. We evaluate here whether mobile exposures of passive samplers can provide reliable estimates of dissolved contaminant concentrations. Mobile exposures were obtained by towing samplers fastened to the end of a benthic trawl net. Significant and reproducible absorption of polycyclic aromatic hydrocarbons during 5 h-long deployments was made possible by high sampling rates resulting from high water turbulences during towing at 1.2-1.5 knots. Sampling rates (72-215 L d⁻¹) estimated from the dissipation of performance reference compounds were supported by in situ calibration with samplers exposed for a 30 days in the vicinity of the test site. Higher fluoranthene and pyrene absorption in samplers exposed to the trawling-induced sediment plume could be attributed to desorption from re-suspended sediments. This mode of exposure has the potential to be used in monitoring programmes.     

纳滤膜深度处理棉针织品印染废水

采用芳香聚酰胺膜(NF-1#)、复合膜(NF-2#)和聚酰胺复合膜(NF-3#)深度处理棉针织品印染废水，考察了膜分离性能及膜污染情况的影响因素。实验结果表明，在操作压力为0.5MPa、废水温度为25~35℃、废水pH为7的条件下，NF-1#膜处理效果最佳，COD去除率最高，为76.0%~85.0%;脱盐率也最高，达90.0%。膜过滤后浓水送污水厂处理，产水回用于车间生产。操作压力增高、废水温度升高和废水pH增大均导致滤饼层阻力(Rc)和膜过滤过程中的总阻力(Rt)增加，Rc是Rt的主要组成部分，同时也是导致膜透过通量下降的主要因素。     

MBR工艺中溶解性有机物的分子量和EEM解析

采用凝胶过滤色谱(GFC)分子量测定技术和三维荧光(EEM)光谱技术,对平板膜-生物反应器工艺应用于餐饮废水和粪便污水处理的工程实例进行研究,对比分析2套工艺中的调节池水和出水的溶解性有机物(DOM)及污泥胞外聚合物(EPS)的性质变化.研究表明,餐饮废水处理过程的调节池水DOM中大分子(＞100 kDa)物质比例为6...     

摇动床生物膜反应器和活性污泥法组合技术处理高浓度有机废水的研究

利用摇动床生物膜反应器(简称摇动床)技术具有的容积负荷高与污泥产量低的优点,在普通活性污泥池的前部填充高性能丙烯酸树脂纤维(Biofringe)填料,研究了摇动床和活性污泥法组合技术处理高浓度有机废水的有效性。结果表明,该组合技术具有很强的有机物去除能力,当进水COD平均质量浓度由1500mg/L上升到2514mg/L时,出水COD的平均去除率基本保持在96%以上;整个运行阶段的出水COD浓度均满足《污水综合排放标准》(GB8978—1996)的二级标准;当进水NH4+-N浓度增加时,NH4+-N的去除率由99.7%降低到76.5%,但是在试验运行的整个阶段,摇动床和活性污泥法组合技术系统都表现出较强的硝化能力;活性污泥池中最高的混合液悬浮固体(MLSS)质量浓度为10625mg/L,最高MLSS约为普通活性污泥法的4倍;运行结束后的污泥产率为0.186,污泥产率仅为普通活性污泥法的50%左右。     

高效聚合氯化铝对超滤膜污染影响的中试研究

针对某水厂以超滤为核心的短流程水处理工艺,在通过聚氯乙烯(PVC)超滤膜之前选择不同投加量(5、10、15和20 mg/L)的高效聚合氯化铝(HPAC)对长江下游原水进行混凝处理。通过跨膜压差(TMP)增长趋势、CODMn的去除率以及混凝后的水质,可知HPAC的最优投加量为15 mg/L。在此投加量下,运用体积排阻色谱法分析原水、膜前水、膜后水中各相对分子质量有机物的变化,可以发现混凝去除有机物的效果要优于超滤截留的。继而将HPAC与另外4种常用混凝剂:硫酸铝(分析纯)、氯化铁(化学纯)、聚合氯化铝(PAC)、聚合硫酸铁进行对比,结果表明,在它们各自最优投加量下,HPAC能够更有效地减缓超滤膜TMP的增长率,从而降低膜污染。因此,认为HPAC是与PVC超滤合金膜契合效果最佳的混凝剂。     

BOD微生物膜的再利用研究初探

对失去大部分活性的微生物膜进行再培养，以研究膜再利用的可能性。试验结果初部表明：在1／2MS培养基中加入一定量的植物激素，不仅可以使膜的电位值（I0）显著升高，且活性强，稳定性好，可使膜重复利用。     

Influence of Relative Humidity and Ozone on the Sampling of Volatile Organic Compounds on Carbotrap/Carbosieve Adsorbents

By using a dynamic dilution system, the atmospheric measurement of 11 selected toxics VOCs (ethylene, acetylene, propene, 1-butene, 1,3-butadiene, 1-pentene, 1-hexene, benzene, toluene, ethylbenzene, m+p-xylene) from the list WHO of 1996 and TO-14 method of US EPA by preconcentration by thermal desorption (TD), analysis by gas chromatography (GC), identification and quantification with a flame ionisation detector (FID) was developed and validated in term of metrology, especially the techniques of sampling of these VOCs with adsorbents cartridges "Air Toxics" when used with an "UMEG sampler" equipped in the inlet with a nafion membrane. In particular the influence of climatic conditions (temperature and relative humidity) and the influence of chemical factors like ozone, on the representativity of sampling were studied. Experiments made with various humidities showed that the addition of a nafion membrane in the inlet of the sampling system was required. Without this membrane, losses of compounds were observed for RH >50%. With this membrane, storage for 2 weeks in a refrigerator, as for canisters, did not induce a loss of compounds. No significative decrease of concentrations of the studied VOCs after 14 days storage, which are known to react with ozone, were observed with an ozone concentrations of 55 ppb. One explanation is that nafion membrane, placed in the inlet of the sampler, will neutralize ozone before entering the sampling tubes. This observation is in accordance with literature which states that the sampling of VOCs on Carbotrap cartridges without ozone scrubber induce a loss of compounds.     

序批式动态膜生物反应器处理低碳氮比废水的试验研究

以序批式动态膜反应器为研究对象,对其处理低碳氮比废水的效果进行了试验研究.试验温度为19 ～ 21℃,MLSS为3～5g/L;好氧阶段溶解氧质量浓度为2 ～4 mg/L,厌氧阶段溶解氧质量浓度为0.2～0.5 mg/L;水力停留时间共12 h,其中好氧阶段8h,厌氧阶段4h.结果表明:当进水COD、TN和NH4+-N质量浓度分别为250～300mg/L、103 ～ 156 mg/L和92～140 mg/L时,反应器对上述污染物表现出较高且稳定的去除效率,COD、TN和NH4+-N平均去除率分别达到76.15％、82.16％和90.13％.同时,反应器系统中污泥的比硝化速率与常规处理装置中的活性污泥相比较高,以NH4+-N的降解量计为0.101 d-1,以NO3--N的积累量计为0.091 d-.     

软/硬质悬浮填料对MBR中EPS的影响

以聚丙烯无纺布为膜组件,向浸渍式膜生物反应器(MBR)中分别投加硬/软质悬浮填料处理人工废水.分析测定EPS、SVI、膜污染阻力及跨膜压力的变化,采用统计分析方法研究了软/硬质悬浮填料对MBR中EPS及SVI的影响;通过扫描电镜(SEM)分析,表征添加软/硬质悬浮填料膜表面的污染状况.结果表明,添加软/硬质悬浮填料膜组件表面滤饼中的溶解性EPSS和结合性EPSB与膜污染阻力的皮尔逊相关系数(rp)分别为0.929～ 0.984和0.798～0.853,EPSS与膜污染阻力之间表现出更强的相关性,EPSS对膜污染阻力的贡献大于EPSB.添加软/硬质悬浮填料MBR污泥混合液的EPS与SVI的皮尔逊系数(rp)分别为0.895和0.798,呈现明显的正相关性.SEM分析也表明,添加软质填料的膜表面污泥覆盖程度大于硬质填料的膜表面,但膜内部的污泥沉积量明显低于硬质填料.与软质悬浮填料相比,硬质悬浮填料能导致MBR污泥混合液的SVI和EPS含量增大,增加膜污染速率和不可逆膜污染阻力,软质悬浮填料具有更好的控制膜不可逆污染的效能.