原子吸收法间接测定水中微量钛

用三正辛基膦化氧（ＴＯＰＯ）－环乙烷萃取钛，使用Ｔ型毛细管－根喷雾有机相，另一根喷雾４０ｍｇ／ＬＣａ溶液，用Ｃａ灯通过测量干扰元素被对干扰元素测定的影响对Ｔｉ进行间接测定，方法最佳线性范围０．５～３．０ｍｇ／Ｌ，加收率９０％～１０２％之间，相结标准偏差为２．８％～３．８％。     

Fe~（2＋）－H_2O_2法处理DSD酸生产氧化母液的研究

为改善ＤＳＤ酸氧化母液的可生化降解性，将废液先用有机絮凝剂ＴＳ－１（一种季胺盐）处理，ＴＳ－１的投加量为３ｇ／Ｌ，其后用Ｆｅ２＋－Ｈ２Ｏ２法氧化，Ｆｅ２＋和Ｈ２Ｏ２的量分别为１５０ｍｇ／Ｌ，７ｇ／Ｌ，废液ＣＯＤ和色度的去除率分别可达６４％和６２％。经处理后的废水，其ＢＯＤ５／ＣＯＤ≈０．３，可以认为已达到生化处理的要求。当Ｈ２Ｏ２的投量为２ｇ／Ｌ，经Ｆｅ２＋－Ｈ２Ｏ氧化处理后的废液，再用ＦｅＣｌ３进行两级混凝处理（ＦｅＣｌ３的投加量分别为ｓｇ／Ｌ和２ｇ／Ｌ），则ＣＯＤ和色度的去除率可达９０％和９５％。     

热带海洋环境中BHC和DDT的行为特征研究：Ⅰ.中国珠江口区旱季BHC…

本文物１９９４年１１月用气相色谱法研究了旱季珠江口区环境中ＢＨＣ和ＤＤＴ的含量与分布。结果表明，表层海水ＢＨＣ含量为０．０８７μｇ／Ｌ，ＤＤＴ为０．０８０μｇ／Ｌ；底层海水ＢＨＣ为０．１１７μｇ／Ｌ，ＤＤＴ为０．５０６μｇ／Ｌ。沉积物ＢＨＣ为１１．１５×１０＾－９（干），ＤＤＴ为３３．４６×１０＾－９（干）。海水中的盐度、ＤＯ、ＣＯＤ与其ＢＨＣ、ＤＤＴ含量之相关性没有规律，沉积物中微生物的含量与Ｂ     

活性污泥处理系统耐含盐废水冲击负荷性能

不同含盐量的废水对运行正常的活性污泥处理系统的冲击影响试验结果表明：当处理生活污水的活性污泥系统受到的ＮａＣｌ冲击负荷小于５ｇ／Ｌ时,系统不会受到太大的影响,活性污泥的氧摄入速率（ＯＵＲ）和系统的总有机碳（ＴＯＣ）去除率仍能够保持正常;冲击负荷大于１０ｇ／Ｌ后,盐对活性污泥产生影响,活性污泥ＯＵＲ降低约３５％ ,ＴＯＣ去除率降低约３０％     

阳极溶出伏安法测定水体中痕量Sb^5＋

在ｐＨ３．４，８－羟基喹啉、甲基橙的浓度分别为４３μｍｏｇ／Ｌ、１３μｍｏｌ／Ｌ的０．１ｍｏｌ／Ｌ（ＮＨ４）２ＳＯ４底液中，用阳极溶出伏安法直接测定水体中Ｓｂ＾５＋。其线性范围为０．２６～５．２ｎｍｏｌ／Ｌ，方法的检出限为０．１ｎｍｏｌ／Ｌ；９次重复测定的变异系数为０．８％；回收率为９５．６％～１０４％。大部分常见阳离子不干扰测定。     

A／BAC－SRB工艺对有机磷农药生产废水处理的研究

采用Ａ／ＢＡＣ－ＳＲＢ工艺对有机磷农药生产废水的处理进行了研究。按正交试验优选的工艺参数操作，当进水化学需氧量（ＣＯＤｃｒ）为２０１２ｍｇ／Ｌ生化需氧量（ＢＯＤ５）为３４４ｍｇ／Ｌ，总磷（Ｔ－Ｐ）为２５０ｍｇ／Ｌ，有机磷（Ｏ－Ｐ）为１３２ｍｇ／Ｌ时，其总去除率分别为９５％、８０％、７０％和５５％。该工艺最大的优点是耐毒能力强，剩余污泥少，处理效率高。     

A／BAC—SRB工艺对有机磷农药生产废水处理的研究

采用Ａ／ＢＡＣ－ＳＲＢ工艺对有机磷农药生产废水的处理进行了研究。按正交试验优选的工艺参数操作，当进水化学需氧量（ＣＯＤｃｒ）为２０１２ｍｇ／Ｌ，生化需氧量（ＢＯＤ５）为３４４ｍｇ／Ｌ，总磷（Ｔ－Ｐ）为２５０ｍｇ／Ｌ，有机磷（Ｏ－Ｐ）为１３２ｍｇ／Ｌ时，其总去除率分别为９５％，８０％，７０％和５５％。该工艺最大的优点是耐毒能力强，剩余污泥少，处理效率高。     

水中可吸附有机硫(AOS)的测定——离子色谱法

使吸附在活性炭上的有机硫化物在高温氧气流中燃烧、分解、定量地转化为无机硫的氧化物，经硼砂双氧水溶液吸收，生成硫酸根离子，用离子色谱法分离测定．可测定ＡＯＳ的范围为２５～１３３３μｇ／Ｌ，回收率为８６．６％，相对标准偏差小于１０％（ｎ＝３５）用该方法还可同时测定水中的可吸附有机氯．     

水解(酸化)-缺氧-好氧固定床生物膜系统处理焦化废水的试验研究

用内填ＹＤＴ弹性立体填料的水解（酸化）－缺氧－好氧固定床生物膜系统焦化废水。结果：当进水ＣＯＤ和ＮＨ３－Ｎ浓度分别为１０６５ｍｇ／Ｌ和２５３ｍｇ／Ｌ,系统水力停留时间（ＨＲＴ）为３３．５ｈ,混合液回流比为３．６时,出水ＣＯＤ约为１８０ｍｇ／Ｌ,ＮＨ３－Ｎ为５ｍｇ／Ｌ,ＣＯＤ和ＮＨ３－Ｎ的去除率分别达８３％和９８％。     

水解（酸化）－缺氧－好氧固定床生物膜系统处理焦化废水的试验研究

用内填ＹＤＴ弹性立体填料的水解（酸化）－缺氧－好氧固定床生物膜系统处理焦化废水。结果表明：当进水ＣＯＤ和ＮＨ３－Ｎ浓度分别为１０６５ｍｇ／Ｌ和２５３ｍｇ／Ｌ，系统水力停留时间（ＨＲＴ）为３３．５ｈ，混合液回流比为３．６时，出水ＣＯＤ约为１８０ｍｇ／Ｌ，ＮＨ３－Ｎ为５ｍｇ／Ｌ，ＣＯＤ和ＮＨ３－Ｎ的去除率分别达８３％和９８％。     

Evaluation of N-acetylcysteine and glutathione as quenching agents for the analysis of halogenated disinfection by-products

Disinfection by-products (DBPs), formed from the reactions of disinfectants with natural organic matter and halides in drinking water, were considered to be cytotoxic and genotoxic, and might trigger various cancers. The relatively low concentration of DBPs in finished water (low µg/L or even ng/L levels) and the interference from water matrix inhibited in situ determination of DBPs. Moreover, the further formation and degradation of DBPs by disinfectants during the holding time (several hours to several days) from sample collection to analysis could adversely affect the determination of DBPs. To obtain accurate, precise and reliable data of DBP occurrence and formation, robust and reliable sample preservation is indispensable. However, the commonly used quenching agents (e.g., sodium sulfite, sodium thiosulfate, and ascorbic acid) for sample preservation can decompose reactive DBPs by reductive dehalogenation. This study evaluated the performance of N-acetylcysteine (NAC) and glutathione (GSH) as quenching agents for the analysis of halogenated DBPs by investigating the stoichiometry of the disinfectant-quenching agent reaction, the formation of DBPs during chlor(am)ination of NAC or GSH, and the effects of NAC or GSH on the stability of 18 individual DBPs and total organic halogen (TOX). Based on the results of this study, NAC and GSH were considered to be ideal quenching agents for the analysis of most DBPs and TOX, except halonitromethanes.     

Determination of gaseous semi- and low-volatile organic halogen compounds by barrier-discharge atomic emission spectrometry

A group parameter approach using "total organic halogen" is effective for monitoring gaseous organic halogen compounds, including fluorine, chlorine, and bromine compounds, generated from combustion. We described the use of barrier-discharge radiofrequency- helium-plasma/atomic emission spectrometry, for the detection of semi- and low-volatile organic halogen compounds (SLVOXs), which can be collected by Carbotrap TM adsorbents and analyzed using thermal desorption. The optimal carrier gas flow rates at the injection and desorption lines were established to be 100 mL/min. The detection range for SLVOXs in the gaseous samples was from 10 ng to tens of micrograms. Measuring F was more difficult than measuring Cl or Br, because the wavelength of F is close to that of air. The barrier- discharge radiofrequency-helium-plasma/atomic emission spectrometry measured from 85% to 103% of the SLVOXs in the gas sample. It has been found that Carbotrap B is appropriate for high-boiling-point compounds, and Carbotrap C is suitable for the determination of organic halogen compounds with lower boiling points, in the range 200-230°C. Under optimal analysis conditions, a chlorine- containing plastic was destroyed using different oxygen concentrations. Lower oxygen concentrations resulted in the production of lower amounts of organic halogen compounds.     

Effect of ferric and bromide ions on the formation and speciation of disinfection byproducts during chlorination

The e ects of ferric ion, pH, and bromide on the formation and distribution of disinfection byproducts (DBPs) during chlorination were studied. Two raw water samples from Huangpu River and Yangtze River, two typical drinking water sources of Shanghai, were used for the investigation. Compared with the samples from Huangpu River, the raw water samples from Yangtze River had lower content of total organic carbon (TOC) and ferric ions, but higher bromide concentrations. Under controlled chlorination conditions, four trihalomethanes (THMs), nine haloacetic acids (HAAs), total organic halogen (TOX) and its halogen species fractions, including total organic chlorine (TOCl) and total organic bromide (TOBr), were determined. The results showed that co-existent ferric and bromide ions significantly promoted the formation of total THMs and HAAs for both raw water samples. Higher concentration of bromide ions significantly changed the speciation of the formed THMs and HAAs. There was an obvious shift to brominated species, which might result in a more adverse influence on the safety of drinking water. The results also indicated that high levels of bromide ions in raw water samples produced higher percentages of unknown TOBr.     

高蛋白有机废弃物厌氧消化系统稳定性及其耐氨氮机制解析

病死及自然灾害产生的大量畜禽尸体的不恰当处理处置会带来较为严重的环境卫生和公众安全隐患.本研究利用厌氧消化技术对畜禽尸体这类高蛋白有机废弃物的无害化处理进行尝试,旨在探索其适宜的有机负荷条件、系统的稳定性及潜在的氨抑制风险.研究表明高蛋白有机废物(以猪肉作为实验样品)作为厌氧消化基质时,系统稳定运行的有机负荷能够达倒(4.76±0.41)kg·m~(-3)·d~(-1);同时,VS降解率、单位体积沼气产率、单位添加VS沼气产率、单位降解VS沼气产率以及甲烷含量分别能达到95%、(3.72±0.21)L·L~(-1)·d~(-1)、(0.78±0.02)m~3·kg~(-1)、(0.82±0.02)m~3·kg~(-1)以及65%.在该条件下,TAN和FAN的浓度与系统产气性能没有直接线性关系,且在浓度高达5700 mg·L~(-1)和700 mg·L~(-1)时未呈现对系统的明显抑制作用.454高通量焦磷酸测序法对系统内古菌种群相对密度的分析结果表明,系统中氨抑制问题得到一定程度的缓解或者消除的原因可能为甲烷八叠球菌属(Methanosarcina)的优势地位并未受到明显影响,以及整个产甲烷菌种群在系统运行过程所得到的明显驯化.     

Fenton氧化去除制药企业活性污泥中AOX的效果研究

用Fenton氧化处理合成制药企业活性污泥混合液,考察了不同Fe~(2+)、H_2O_2投加量和不同反应时间下污泥与上清液中AOX(可吸附有机卤代物)的去除效果,优化了反应条件,探讨了氧化机制.结果表明,Fenton氧化的最佳条件为H_2O_2投加量0.90 mol·L~(-1),Fe~(2+)投加量0.045 mol·L~(-1)[物质的量比为:n(Fe~(2+))∶n(H_2O_2)=1∶20],反应2 h,污泥和上清液中AOX可分别去除70.7%和78.5%.GC-MS分析结果显示,污泥中含有11种有机卤代物,Fenton氧化后有8种不再检出;3种仍有检出,但浓度有所降低,去除率约为40%~50%.与此同时,污泥中对二甲苯、邻苯二甲酸二异丁酯等非有机卤代物类有毒有害有机物也得到有效去除.     

长期施肥对棕壤有机碳储量及固碳速率的影响

利用棕壤肥料长期定位试验,研究了不同施肥条件下棕壤有机碳在0~60 cm土层的含量和储量特征以及土壤固碳速率.试验共设6个处理,即氮磷肥有机肥配施(M_2NP)、氮肥有机肥配施(M_2N)、单施有机肥(M_2)、单施氮肥(N)、氮磷肥配施(NP)和不施肥处理(CK).结果表明:经过31年长期不同施肥,各处理土壤有机碳(SOC)含量和储量的剖面分布均呈现随土层深度增加而显著降低的规律.本试验条件下M_2NP、M_2N、M_2、NP、N、CK处理的耕层有机碳富集系数分别为0.465、0.455、0.407、0.48_2、0.393、0.471,表明耕层土壤对有机碳的保持强度最强.在0~60 cm土层土壤有机碳储量表现为M_2NP、M_2NM_2、NPNCK,有机肥和化肥配施能够显著提高土壤有机碳含量和储量.与试验前相比,CK处理各土层土壤有机碳含量和储量均显著降低.各处理碳库管理指数(CPMI)表现为M_2NPM_2NM_2NNPCK.分析不同施肥处理土壤固碳速率可知,与试验前相比,CK处理表现为碳的净释放,固碳速率达-401.4 kg·hm~(-_2)·a~(-1);固碳速率最高的为M_2NP,M_2N,分别达到489kg·hm~(-_2)·a~(-1)、440._2 kg·hm~(-_2)·a~(-1).综合结果表明,化肥、有机肥配施所产生交互效应更有利于棕壤有机碳储量的增加及固碳速率的提高.     

Fenton氧化深度处理石化废水厂二级出水研究

采用连续流Fenton氧化对石化废水处理厂二级出水进行了处理试验,研究了药剂投量对COD及磷处理效果的影响,同时对处理过程中有机物的变化特性进行了分析.结果表明,原水COD平均为64.8 mg·L-1,PO3-4-P平均为0.79 mg·L-1,当H2O2(30%)投加量为0.4 m L·L-1,Fe SO4·7H2O的投加量为0.8 g·L-1,PAM投加量为0.9 mg·L-1,停留时间为30 min时,COD的平均去除率为24.3%,出水COD低于50 mg·L-1,PO3-4-P平均去除率为95.5%,原水中相对分子质量小于1×103的有机物占80.4%,Fenton氧化处理后该部分比例增加至95.6%.三维荧光分析结果表明,Fenton氧化对水中蛋白类、酚类去除效果显著.GC-MS结果表明,石化二级出水中检出主要有机物约117种,氧化后检出27种,含不饱和键类有机物去除明显.Fenton氧化可用于石化二级出水的深度处理.     

溶解性有机质对罗红霉素光降解的影响研究

近年来,罗红霉素(ROX)因其用量大、检出频率高和生态风险大引起了广泛关注.本文主要研究了环境pH条件下不同的溶解性有机质(DOM),包括富里酸(PLFA)、腐殖酸(SRHA)和天然有机质(SRNOM)对罗红霉素光降解的影响及主要活性物种对其光降解的贡献.结果表明:纯水中罗红霉素可发生自敏化光降解,在pH 6～8条件下,罗红霉素光降解的一级反应速率常数为0.0033～0.0049 h~(-1).DOM促进了罗红霉素光降解,其促进效果从大到小为PLFASRNOMSRHA.DOM共存时罗红霉素光降解的反应速率常数随pH增加而增加,在pH 6时为0.0145～0.0266 h~(-1),在pH 8时为0.0273～0.0577 h~(-1).通过异丙醇淬灭实验发现,羟基自由基(·OH)对罗红霉素光降解起主要贡献,其贡献率在pH 6时为83.45%～98.70%,在pH 8时降低至76.76%～78.02%;3种DOM体系中产生的单态氧(~1O_2)的稳态浓度在(5.15～7.86)×10~(-14) mol·L~(-1)范围内;在pH 6、7和8的条件下,~1O_2与罗红霉素的二级反应速率常数分别为2.27×10~5、1.96×10~6和1.51×10~7 L·mol~(-1)·s~(-1).~1O_2对罗红霉素的光降解的贡献随pH升高而升高,在pH 6时为0.21%～0.43%,在pH 8时为4.85%～11.33%.     

缙云山不同土地利用方式下土壤团聚体中活性有机碳分布特征

于缙云山阳坡同一海拔高度处选择了亚热带常绿阔叶林(简称林地)、荒地、坡耕地和果园4种土地利用方式,在0~60 cm的土壤深度内每隔10 cm采集一个土壤样品,测定大团聚体(2 mm)、中间团聚体(0.25~2 mm)、微团聚体(0.053~0.25 mm)以及粉+黏团聚体(0.053 mm)这4种粒径团聚体内的土壤活性有机碳(labile organic carbon,LOC)的含量,分析缙云山不同土地利用方式对团聚体LOC的影响.结果表明,各粒径团聚体中LOC含量均随土壤深度的增加而显著降低,呈现出明显的垂直递减性;在0~60 cm土壤深度的各土层上,基本上均表现为林地和撂荒地各粒径团聚体中LOC含量高于坡耕地和果园.采用土壤等质量方法计算LOC储量,显示大团聚体LOC储量为林地(3.68 Mg·hm-2)撂荒地(1.73 Mg·hm-2)果园(1.43 Mg·hm-2)坡耕地(0.54 Mg·hm-2);中间和微团聚体LOC储量为撂荒地(7.77 Mg·hm-2和5.01 Mg·hm-2)林地(4.96 Mg·hm-2和2.71 Mg·hm-2)果园(3.55 Mg·hm-2和2.10 Mg·hm-2)坡耕地(1.68 Mg·hm-2和1.35 Mg·hm-2);粉+黏团聚体LOC储量为撂荒地(4.32 Mg·hm-2)果园(4.00 Mg·hm-2)林地(3.22 Mg·hm-2)坡耕地(2.37Mg·hm-2).除粉+黏团聚体LOC储量略低于果园外,林地和撂荒地其他粒径团聚体LOC储量均高于果园和坡耕地,表明林地开垦为果园和坡耕地会导致LOC的降低,而坡耕地撂荒则会促进LOC的增加.林地和荒地LOC主要分布在中间团聚体,而果园和坡耕地则为粉+黏团聚体内LOC储量最高,表明在土地利用的转变过程中,粒径较大的团聚体更容易积累或损失LOC.4种土地方式下各粒径团聚体中LOC分配比例随土壤深度的增加而降低,果园和坡耕地各粒径团聚体内LOC分配比例略高于林地和撂荒地,表明林地和撂荒地土壤有机碳(soil organic carbon,SOC)性质更稳定,更有利于碳在土壤中的留存,从而减少SOC矿化分解向大气的释放.相关分析表明,土壤团聚体LOC含量与土壤团聚体总有机碳含量呈极显著正相关关系,表明团聚体LOC可以作为衡量西南地区山地土壤团聚体有机碳动态的一个敏感性指标.     

Determination of selected semi-volatile organic compounds in water using automated online solid-phase extraction with large-volume injection/gas chromatography/mass spectrometry

A rapid, sensitive, and cost-effective analytical method was developed for the analysis of selected semi-volatile organic compounds in water. The method used an automated online solid-phase extraction technique coupled with programmed-temperature vaporization large-volume injection gas chromatography/mass spectrometry. The water samples were extracted by using a fully automated mobile rack system based on x-y-z robotic techniques using syringes and disposable 96-well extraction plates. The method was validated for the analysis of 30 semivolatile analytes in drinking water, groundwater, and surface water. For a sample volume of 10 mL, the linear calibrations ranged from 0.01 or 0.05 to 2.5 μg·L⁻¹, and the method detection limits were less than 0.1 μg·L⁻¹. For the reagent water samples fortified at 1.0 μg·L⁻¹ and 2.0 μg·L⁻¹, the obtained mean absolute recoveries were 70%–130% with relative standard deviations of less than 20% for most analytes. For the drinking water, groundwater, and surface water samples fortified at 1.0 μg·L⁻¹, the obtained mean absolute recoveries were 50%–130% with relative standard deviations of less than 20% for most analytes. The new method demonstrated three advantages: 1) no manipulation except the fortification of surrogate standards prior to extraction; 2) significant cost reduction associated with sample collection, shipping, storage, and preparation; and 3) reduced exposure to hazardous solvents and other chemicals. As a result, this new automated method can be used as an effective approach for screening and/or compliance monitoring of selected semi-volatile organic compounds in water.