污水厂出水DOM的分级及三卤甲烷生成势研究

研究目的在于调查寒冷季节城市污水处理厂出水中天然有机物化学组分分级,探讨各分级组分与消毒副产物生成潜能间之关系。采集污水厂二级出水,以三种不同树脂把污水厂出水中有机物分离成六类不同组分,其中A水厂含量最高的物质为亲水酸性物质(33%)而B水厂的疏水性中性物质含量最多约占总有机物的64%。从总体来看两水厂的疏水性物质含量大于亲水性物质含量,疏水性物质的三卤甲烷生成势也较大,是水体中消毒副产物的主要前驱物质。疏水性有机物质较多,代表受生活污水污染严重,得知该城市污水主要受民生污染较多。     

长江沿线城市水源氯(胺)化消毒副产物生成潜能研究

以长江上游重庆、中游武汉、下游上海等大城市的长江饮用水源为研究对象,在对溶解性有机物分子量和亲疏水性分离的基础上,分别采用氯和氯胺两种方式消毒,对比分析了相同时期沿江这些城市原水中氯(胺)化常规和新兴含氮消毒副产物生成潜能的分子组成规律.研究表明,重庆、武汉、上海三地的溶解性有机物均以小分子前体物为主,主要分布在<1kDa的区间内,且以强疏水性成分和亲水性成分为主,原水经氯(胺)化可产生三卤甲烷、卤乙酸、卤乙腈、三氯硝基甲烷等类型的消毒副产物;三地的氯(胺)化主要的含碳消毒副产物(C-DBPs)和含氮消毒副产物(N-DBPs)生成潜能均在<1kDa的区间内最大,从上游到下游,在<1kDa的区间内的生成潜能占各自总潜能比例逐渐增加.三地的氯(胺)化的C-DBPs和N-DBPs生成潜能均以强疏水性组分或亲水性组分为主,且氯胺化可导致亲水性组分C-DBPs和N-DBPs生成潜能所占总量比例增加.     

焦化废水尾水O3氧化消除消毒副产物生成潜能的影响分析

焦化废水经生化处理后的尾水中含有多种溶解性有机物(DOM),可能成为消毒副产物的前体物,进而影响受纳水体下游给水厂的水质安全.因此,对焦化废水外排水(尾水)的消毒副产物生成潜能进行了分析,以实际焦化废水厂尾水为基质,采用气相色谱(GC)考察了O3氧化深度处理前后卤乙腈和三卤甲烷的生成潜能,并结合分子质量分布法和三维荧光光谱法分析了O3氧化处理尾水过程中前体物的转化规律.GC结果表明,焦化废水尾水各个分子质量范围的卤乙腈和三卤甲烷生成潜能分别达到1950.5～3965.1μg.L-1和1498.2～2571.2μg.L-1,表明工业废水排放之前需要考虑其对水体消毒副产物生成潜能的贡献.O3氧化作用可以实现尾水中消毒副产物前体物的削减,相同反应时间的条件下O3浓度越高其削减越有效.溶解性有机碳(DOC)及在254nm波长下的吸光度值(UV254)分析结果表明,O3氧化能部分矿化尾水中的有机物,并优先分解不饱和芳香性有机组分.分子质量和荧光光谱分析结果表明,O3氧化优先矿化小分子组分(<1kDa),并将尾水中大分子有机物分解为小分子(<1kDa),对活泼基团进行预氧化,从而实现氯消毒副产物生成潜能的削减.     

南水北调中线工程总干渠河南段原水中消毒副产物前体物变化规律

以取自南水北调中线总干渠河南段沿线10个分水口门的原水为研究对象,探究了原水中有机物的相对分子质量分布和亲疏水性分布规律;并且研究了原水在氯化和氯胺化条件下消毒副产物生成潜能的变化规律.分离实验结果表明,南水北调沿程原水中的有机物以小分子和强疏水性为主,1×103区间的溶解性有机碳(DOC)所占的比例最大,质量分数约为57%,强疏水性组分的DOC含量最高,占到总量的50%左右;氯化及氯胺化消毒副产物生成潜能分析实验结果表明,氯化及氯胺化后主要生成了两种含碳消毒副产物(三氯甲烷和一溴二氯甲烷)和两种含氮消毒副产物(二氯乙腈和三氯硝基甲烷).氯化三氯甲烷生成潜能约为120μg·L-1,与氯化生成潜能相比,氯胺化三氯甲烷生成潜能减少了90%左右,一溴二氯甲烷减少了84.9%左右,生成的两种含氮消毒副产物增加了,其中二氯乙腈的生成量增加了约2.3倍,但总含氮消毒副产物生成潜能仍旧较低,均小于6μg·L-1.本研究成果可为南水北调中线工程河南段沿线城市的水厂工艺选择和优化提供有效的理论和技术支持.     

石化污水厂二级出水溶解性有机物分级解析研究

以某石化污水处理厂二级出水为研究对象,采用大孔吸附树脂将污水中溶解性有机物分离成亲水性物质、疏水酸性物质、疏水中性物质和疏水碱性物质4个组分,分析了各组分的有机物的组成特征、三维荧光光谱特征及红外光谱特征.结果表明,亲水性物质和疏水酸性物质分别占水样中溶解性有机碳的49%和29%,是该石化污水厂二级出水中的主要物质类别.亲水性物质中含有较多的生物源腐殖质类物质,疏水中性物质含有较多的芳香族蛋白质和溶解性微生物代谢产物类物质.4种组分的红外光谱图中600~1200cm-1波数的指纹区波峰数量最多,多为芳香类同分异构体化合物.     

南方某水源水中天然有机物的特点及氯胺对氯化消毒副产物的控制

在对天然有机物分类的基础上进行了水体中有机物的特性研究，并采用氯胺对不同特性有机物的氯化消毒副产物进行了控制研究。结果表明，疏水酸占有机物总量的24％，疏水中性物质占41％，疏水性有机物占67％；对于三卤甲烷类消毒副产物生成势，疏水酸所产生的最多，疏水碱次之，亲水酸最少；对于卤乙酸类消毒副产物生成势，疏水碱产生的三卤乙酸最多，其次为疏水酸，亲水酸最少。氯胺对不同类有机物氯化消毒副产物控制程度不同，氯胺对疏水中性物质控制三卤甲烷类消毒副产物最好，其次是疏水碱和亲水碱；对疏水酸的三卤甲烷生成量控制较弱，对亲水酸的控制效果最差；氯胺对亲水碱氯化产生卤乙酸的控制效果最好，其次是疏水碱，控制效果最差的为疏水中性物质。     

人工地下水回灌过程中溶解性有机物的去除及变化

在实验室通过模拟土壤柱研究了人工地下水回灌过程中溶解性有机物的去除及其三卤甲烷生成势和三卤甲烷生成活性的变化.利用XAD树脂将回灌水中的溶解性有机物分为3个部分：疏水性有机酸、过渡亲水性有机酸和亲水性有机物.疏水性有机酸的三卤甲烷生成活性高于过渡亲水性有机酸和亲水性有机物.土壤含水层处理（SAT）对亲水性有机物的去除率为68.51%,对疏水性有机酸和过渡亲水性有机酸的去除率分别为58.64%和41.86%.经SAT系统处理后,溶解性有机物及各有机组分的三卤甲烷生成势减少,而三卤甲烷生成活性升高.疏水性有机酸是生成三卤甲烷的主要有机组分.亲水性有机物在SAT系统进水中的三卤甲烷生成活性较低,但由于含量高,三卤甲烷生成势也较大.而过渡亲水性有机酸由于含量和三卤甲烷生成活性较低,三卤甲烷生成势也较低.     

基于EEMs和DOM分离的荧光特征及DBPsFP研究——以南方某市水源水为例

以南方某市饮用水源地源水为研究对象,利用三维荧光-区域积分法(3D-EEMs-FRI)和DAX-8树脂富集分离技术,研究了水样各组分的溶解性有机物(DOM)组成特征、三维荧光光谱(3D-EEMs)特征;采用生成潜能测试,考察了典型消毒副产物三卤甲烷(THMs)和卤代乙酰胺(HAcAms)生成势以及其与水质指标和荧光强度之间的相关性.结果表明:DOM中疏水性有机物(以UV₂₅₄表征)的比例超过70%.HOB(疏水碱性物质)组分主要含有酪氨酸类蛋白质和色氨酸类蛋白质,而HOA(疏水酸性物质)和HIS(亲水性物质)组分相对于HOB组分则含有较多的紫外区类富里酸.调查水样HOA、HOB、HON和HIS组分的三卤甲烷生成势(THMsFP)分别为151.5~194.1,60.6~65,123.4~189.9和104.1~187.1μg/L,而卤代乙酰胺生成势(HAcAmsFP)分别为2.7~3.7,n.d.~0.1,1.3~3.9和2.2~8.4μg/L,THMs和HAcAms前体物在HOA、HON和HIS组分中的分布比较均匀.UV₂₅₄(R²为0.93)、腐殖化指数(HIX)(R²为0.59)与THMsFP有良好的线性关系,可作为预测组分间THMsFP的指标.UV₂₆₀(R²为0.80)、溶解性有机氮(DON)(R²为0.74)与HAcAmsFP有较强的线性关系,可作为预测HAcAmsFP的参数.Pearson相关性分析显示,类富里酸物质区域(III、V)与THMsFP显著相关,该类物质为组分间THMs的重要前体物.荧光的区域积分可以有效预测组分间THMs和HAcAms的生成势.     

黄河原水中消毒副产物前体物的组成特征及其化学预氧化处理效果对比

以取自河南省郑州市石佛原水厂的黄河原水为研究对象,系统研究了原水中消毒副产物(DBPs)前体物的组成规律,对比分析了3种预氧化剂(高锰酸钾、自由氯和二氧化氯)对原水中DBPs生成潜能的消减规律.试验结果表明:原水中DBPs的前体物均以小分子有机物和疏水性组分(52.51%)为主;分子量小于1 k Da有机物组分是生成含氮消毒副产物(N-DBPs)和三卤甲烷(THMs)的主要前体物;疏水性有机物是生成THMs的主要前体物,亲水性有机物是生成N-DBPs的主要前体物.经Cl2预氧化后,直接生成的DBPs随着自由氯投加量的增加而增加,Cl O2和KMn O4预氧化直接增加DBPs产生量.经3种预氧化剂氧化后,原水中三卤甲烷生成潜能(THMFP)均呈现一定的下降,其降低量依次为Cl O2Cl2KMn O4;然而3种预氧化剂都不能有效的减少含氮消毒副产物生成潜能(N-DBPFP),Cl O2预氧化和Cl2预氧化可增加N-DBPs生成潜能,尤其在较高投加量下,Cl2预氧化将大大增加N-DBPs生成潜能.为有效消减总DBPs生成潜能,水厂可优先采用KMn O4或Cl O2作为预氧化剂处理引黄水库或沉砂池水.     

珠江水体中有机物分布、组成及与消毒副产物生成的关系

以珠江水体为研究对象,利用XAD树脂分离溶解性有机物(DOC)中的腐殖质及其他有机组分.考察了珠江中DOC的质量浓度、组成分布、SUVA254和三卤甲烷生成势(THMFP),并分析有机物的组成与三卤甲烷生成势(THMFP)之间的关系.结果表明,珠江水域在广东省内的DOC质量浓度为0.7～33.0 mg.L-1,THMFP为30.39～1 091.52μg.L-1,两者呈正比例线性相关.在空间分布上,各支流的DOC质量浓度和THMFP均沿下游方向逐渐增加,而腐殖质在DOC中所占的质量分数却沿下游方向逐渐递减.在加氯实验中,腐殖质是珠江中最主要的消毒副产物前驱物(产生了珠江中64.6%的三卤甲烷),其三卤甲烷生成活性(STHMFP)是其他有机组分的2倍以上.另一方面,SUVA254和腐殖质的质量分数呈正比例线性相关,说明SUVA254对珠江水中消毒副产物前驱物也有一定的指示作用.     

厌氧-缺氧-好氧处理出水中溶解性有机物组分的特征分析

本研究利用XAD-8大孔树脂对某城市污水处理厂的厌氧-缺氧-好氧(A2O)工艺出水中的溶解性有机物进行了组分分离,分析了各组分的溶解性有机碳(Dissolved organic carbon,DOC)、紫外-可见光谱和遗传毒性.结果表明,污水中亲水性物质和疏水酸性物质的DOC含量分别占总DOC含量的65%和24%.亲水性物质组分中的芳香族化合物含量显著高于其它组分,但是单位质量的亲水性物质、疏水酸性物质和疏水碱性物质中的芳香族化合物含量相近.污水具有一定的遗传毒性,主要遗传毒性物质为亲水性物质和疏水酸性物质,而疏水碱性物质和疏水中性物质则未检出遗传毒性.     

二级处理出水中溶解性有机物的荧光特性

为研究二级处理出水中溶解性有机物的荧光特性,以沈阳市B污水处理厂为研究对象,利用XAD树脂对二级处理出水中的溶解性有机物(DOM)进行分级分离。按照DOM在不同树脂上的吸附特性将其分为5个部分:疏水性有机酸(HPO-A)、疏水性中性有机物(HPO-N)、过渡亲水性有机酸(TPI-A)、过渡亲水性中性有机物(TPI-N)和亲水性有机物(HPI)。研究结果表明,DOM组分中含有类腐植酸荧光团、类富里酸荧光团、类芳香族蛋白质荧光团和类溶解性微生物代谢产物荧光团,此外,还含有具有多环芳香结构的荧光物质。DOM中的荧光物质主要集中在HPO-N和TPI-N中。类腐植酸荧光团、类富里酸荧光团和类溶解性微生物代谢产物荧光团在TPI-N中的含量最高,而类芳香族蛋白质荧光团在HPO-N中的含量最高。对于HPO-A、TPI-A和TPI-N来说,类富里酸荧光峰的强度最高;类芳香族蛋白质荧光峰是HPO-N的最强峰;类溶解性微生物代谢产物荧光峰是HPI的最强峰。     

冬季不同污水处理工艺对溶解性有机物的去除

以东北地区4个城市污水处理厂为研究对象,考察冬季不同污水处理工艺对溶解性有机物(DOM)组分的去除效果,以及对DOM组分的光谱学特性和卤代活性的影响.利用XAD树脂将DOM分为5个部分:疏水性有机酸(HPO-A)、疏水性中性有机物(HPO-N)、过渡亲水性有机酸(TPI-A)、过渡亲水性中性有机物(TPI-N)和亲水性有机物(HPI).结果表明,A/O法、曝气生物滤池、浮动填料法和A2/O法对DOM都具有较高的去除能力,其中曝气生物滤池对DOM的处理效果最好.经4种污水处理工艺处理后,5种组分的芳香性和三卤甲烷生成活性(STHMFP)均升高.A2/O法对HPO-A和TPI-A的芳香性增强程度最高,而曝气生物滤池对HPO-N,TPI-N和HPI的芳香性增强程度最高.浮动填料法对HPO-A,TPI-A和HPI的STHMFP升高最显著,A2/O法对HPO-N的STHMFP增加最显著,曝气生物滤池对TPI-N的STHMFP升高最显著.4种污水处理工艺对HPI中荧光物质的去除率高于非荧光物质.而对于其他4种DOM组分来说,不同的污水处理工艺对不同荧光峰的改变不相同.     

强化混凝对二级处理出水中溶解性有机物特性的影响

以沈阳市B污水处理厂二级处理出水为研究对象,采用FeCl3.6H2O作为混凝剂,研究了强化混凝对二级处理出水中溶解性有机物(DOM)的卤代活性和荧光特性的影响.按照DOM在XAD树脂上的吸附特性将其分为5个部分:疏水性有机酸(HPO-A)、疏水性中性有机物(HPO-N)、过渡亲水性有机酸(TPI-A)、过渡亲水性中性有机物(TPI-N)和亲水性有机物(HPI).结果表明,强化混凝(混凝剂投加量为80mg.L-1,pH=5.00)对DOC的去除率为55.3%.强化混凝对HPO-A的去除率最高,而对HPI的去除率最低.强化混凝后,HPO-N的三卤甲烷生成活性(STHMFP)上升,而其他4种DOM组分的STHMFP下降.强化混凝能够有效去除类富里酸荧光物质和具有高环数和高聚合度的稠环类芳香性荧光物质.强化混凝对DOM组分的去除率和DOM组分的荧光强度下降率的相关性不显著.     

氯化对二级处理出水中溶解性有机物结构的影响

以哈尔滨市W污水处理厂污水为研究对象,利用XAD树脂对二级处理出水中的溶解性有机物(DOM)进行分级分离.按照DOM在不同树脂上的吸附特性将其分为5个部分:疏水性有机酸(HPO-A)、疏水性中性有机物(HPO-N)、过渡亲水性有机酸(TPI-A)、过渡亲水性中性有机物(TPI-N)和亲水性有机物(HPI).考察了二级处理出水中有机组分的组成分布、三卤甲烷生成势、紫外光谱和红外光谱.结果表明,二级处理出水中的主要成分是HPO-A和HPI,两者含量之和达70.8%.HPO-A是加氯消毒时产生三卤甲烷的主要有机组分,其三卤甲烷生成活性(STHMFP)为232.9μg/mg.而HPO-N、TPI-A、TPI-N和HPI的STHMFP介于100～125μg/mg之间.氯化反应后,HPO-A、HPO-N、TPI-A和HPI的紫外-可见吸光度均降低,而TPI-N则相反.并且HPO-A、HPO-N、TPI-A和TPI-N中的O-H、C=C和苯环的含量降低,而C-O的含量升高,还生成了C=O和C-Cl.     

Removal and transformation of organic matters in domestic wastewater during lab-scale chemically enhanced primary treatment and a trickling filter treatment

To find a simple and economical way for treating the domestic wastewater in small counties and towns, a process combining chemically enhanced primary treatment and a trickling filter (CEPT-TF, representing the physical and biological effects) was constructed and operated in laboratory conditions. The characteristic behaviors of dissolved organic matter in raw wastewater and effluents were examined during steady-state operation. Experimental results showed that the process of CEPT and TF in series was beneficial for the removal of hydrophobic and hydrophilic organics. Specially, the hydrophobic and aromatic materials could be preferentially removed in the CEPT unit, and the hydrophilic fraction in the TF. Structural changes of the organic fractions during the operation of the different units were also characterized via spectrum analysis.     

Organic matter extracted from activated sludge with ammonium hydroxide and its characterization

In order to characterize the organic properties of waste activated sludge in a wastewater treatment plant,organic matter within sludge was extracted with NH 3 ·H 2 O preferentially,and subsequently fractionated into five fractions using XAD-8/XAD-4 resins.Up to a 63.8%-71.1% of organic matter within the sludge could be efficiently extracted by NH 3 ·H 2 O.Fractionation results showed that hydrophobic acid and hydrophilic fraction were two main components among the sludge organic matter (accounting for 32.2% and 48.0% of the bulk organic matter,respectively),whereas transphilic acid,hydrophobic neutral and transphilic neutral were quite low (accounting for 9.2%,5.8% and 4.8%,respectively).Despite that the extractant of NH 3 ·H 2 O showed a relatively higher extraction efficiency of the aromatic components,the relatively low aromaticity of the organic fractions implied that those non-aromatic components could also be effectively extracted,especially for neutral and hydrophilic fractions.In addition,acidic fractions contained more aromatic humic-like components,whereas the neutral fractions had a greater content of aromatic proteins and soluble microbial byproduct-like components.Extraction of sludge organics with NH 3 ·H 2 O and subsequential fractionation using XAD resins could be a novel method for further characterization of sludge organics.     

Fouling of nanofiltration membrane by e uent organic matter: Characterization using di erent organic fractions in wastewater

The UF membrane with molecular weight cuto (MWCO) ranging from 2 to 100 kDa and XAD-8 resin were employed to identify the characteristic of molecular weight (MW) distribution of wastewater e uent organic matter (EfOM) in terms of TOC and UV254, as well as the amounts of the hydrophilic/hydrophobic organic fractions in di erent MW ranges. Then, the nanofiltration (NF) membrane fouling experiments were carried out using the above fractionated water to investigate the e ect of MW distribution and hydrophilic/hydrophobic characteristics of EfOM on the membrane flux decline using the fractionated water samples. The experimental results have shown that 45.61% of the total organics belongs to the low MW one, among which the percentage of the hydrophilic organics with low MW (less than 2 kDa) was up to 28.07%, while that of the hydrophobic organics was 17.54%. In particular, the hydrophilic fraction was found to be the most abundant fraction in the e uents. MW distribution has a significant e ect on the membrane fouling. When the MWwas less than 30 kDa, the lower the MW, the larger was the specific flux decline, while in the case of MW higher than 30 kDa, the higher the MW, the larger was the specific flux decline, and the decline degree of low MW organics was larger than the high MW one. With the same MW distribution range, specific flux decline of the hydrophilic organic was considerably slower than that of the hydrophobic organic, which indicated that the hydrophobic organic fractions dominantly contribute to the flux decline.     

Fouling of nanofiltration membrane by effluent organic matter： Characterization using different organic fractions in wastewater

The UF membrane with molecular weight cutoff (MWCO) ranging from 2 kDa to 100 kDa and XAD-8 resin were employed to identify the characteristic of molecular weight (MW) distribution of wastewater effluent organic matter (EfOM) in terms of TOC and UV254, as well as the amounts of the hydrophilic/hydrophobic organic fractions in different MW ranges. Then, the nanofiltration (NF) membrane fouling experiments were carried out using the above fractionated water to investigate the effect of MW distribution and hydrophilic/hydrophobic characteristics of EfOM on the membrane flux decline using the fractionated water samples above. The experimental results have shown that 45.61% of the total organics belongs to the low MW one, among which the percentage of the hydrophilic organics with low MW (less than 2 kDa) was up to 28.07%, while that of the hydrophobic organics was 17.54%. In particular, the hydrophilic fraction was found to be the most abundant fraction in the effluents. MW distribution has a significant effect on the membrane fouling. When the MW was less than 30 kDa, the lower the MW, the larger was the specific flux decline, while in the case of MW higher than 30 kDa, the higher the MW, the larger was the specific flux decline, and the decline degree of low MW organics was larger than the high MW one. With the same MW distribution range, specific flux decline of the hydrophilic organic was considerably slower than that of the hydrophobic organic, which indicated that the hydrophobic organic fractions dominantly contribute to the flux decline.