SBR法处理化学药物制剂废水

采用 ＳＨＲ法处理化学药物制剂废水． 调节 ｐＨ至７．５,进水 ＣＯＤｃｒ ２２４～１５３０ ｍｍ／Ｌ,曝气１０ ｈ, ＣＯＤｃｒ容积负荷达２．５８ｋｇ／ｍ~３·ｄ,ＣＯＤｃｒ的去除率高达９４．２％,处理后出水ＣＯＤｃｒ＜１００ｍｇ／Ｌ,达到综合排放标准（ＧＢ８９７－９６）一级标准。ＣＯＤｃｒ容积负荷至３．８４ ｋｇ／ｍ~３·ｄ, ＣＯＤｃｒ去除率仍＞８５．９％。     

驯化活性污泥处理明胶有机废水的实验

利用驯化活性污泥对组分复杂的明胶有机废水进行有机物降解实验。结果表明,明胶废水的ＢＯＤ５／ＣＯＤｃｒ比值为０．４４－０．４６,ＣＯＤｃｒ进水浓度在１０００－１２００ｍｇ／Ｌ人,ＣＯＤｃｒ和ＢＯＤ５去除率分别达８１％－８３％和８６％－９１％。     

生化法处理煤气废水

采用Ａ／Ｏ工艺处理煤气废水的研究结果表明,该工艺能同时去除煤气废水中的有机物和氨氮,在试验确定的条件下,该工艺对煤气废水中的ＣＯＤｃｒ去除率达９１．０％,ＢＯＤ５去除率达９９．１％,ＮＨ３－Ｎ去除率达９９．２％,ＴＮ去除率达９４．７％。     

气浮——厌氧——好氧工艺处理高浓度印染废水

根据高浓度印染废水水质特性，开发了气浮－厌氧－好氧处理工艺。并应用于处理工程中，获得了较好的效益。该系统运行结果表明，在进水平均ＣＯＤｃｒ２８８３ｍｇ／Ｌ和设定的ＨＲＴ下，气浮单元出水ＣＯＤｃｒ，为１５３９．０ｍｇ／Ｌ，厌氧池出水１１９２．０ｍｇ／Ｌ，好氧池出水２２５．３ｍｇ／Ｌ，总ＣＯＤｃｒ去除率为９２．２％，处理费用１．７３元／ｔ水，且处理出水可回用于生产，因此该工艺有推广应用的潜力。     

加压生物接触氧化法处理增塑剂生产废水试验研究

主要介绍了采用加压生物接触氧化法处理增塑剂废水。在停留时间为２２ｈ，压力为０．４ＭＰａ，水中溶解氧保持５ｍｇ／Ｌ左右时，进水ＣＯＤＣＲ为１１７００ｍｇ／Ｌ，ＢＯＤ５为６８７３ｍｇ／Ｌ，出水ＣＯＤＣｒ去除率为８９％，ＢＯＤ５去除率为９６％。为增塑剂废水治理工程设计提供了重要参数。     

利福平废水的絮凝和生化处理研究

种福平生产的废水ＣＯＤ高达６万,用ＰＦＳ、Ｃ－ＰＡＭ脱稳,密集网捕式絮凝处理后,ＣＯＤ去除率达２７％,ＢＯＤ５／ＣＯＤｃｒ从０．１９上升到０．３２,絮凝前后水质和色谱分析表明,絮凝后５种有机物去除效率均在２２％以上,使生化处理成为可能,进生化池废水经稀释后,用活性污泥法处理９天后,ＣＯＤ从１．５万降至ＣＯＤ〈３００ｍｇ／Ｌ,达到治理要求。     

几种混凝剂处理煤气洗涤废水的比较

用４种常用的混凝剂Ａｌ２（ＳＯ４）３,ＰＡＣ,ＰＦＳ及ＦｅＳＯ４分别对煤气洗涤废水进行了混凝实验研究,结果表明,使用上述４种药剂对废水ＣＯＤｃｒ最高去除率分别为６３．９％,６７．４％,６１．３％和５７．４％;乳化油去除率分别为７１．６％,７５．６％,７４．８％和７０．５％,浊度去除率分别为９３．４％,９４．１％〈９５．６５和９９．１％,而从经济效益上看,４种药剂去除每ｋｇ废水中ＣＯＤｃｒ所需药剂费     

养猪场废水处理工艺研究

采用接触氧化－水解－两段接触氧化－混凝工艺处理高浓度养殖废水,通过试验得到最佳工艺参数,在最佳试验条件下,进水ＣＯＤｃｒ小于５０００ｍｇ／Ｌ,经处理后出水ＣＯＤｃｒ平均去地９７％,ＢＯＤ５去除率大于９８％,氨氮去除率大于９６％,各项主要指标可达污水综合排放标准一级标准。     

水解——好氧——混凝沉淀工艺处理涤纶厂聚酯废水

报道了用上流式厌氧污泥床和生物接触氧化池对涤纶厂聚酯废水所进行的中试。当上流式厌氧污泥床进水ＣＯＤｃｒ浓度为１２００ｍｇ／Ｌ，经水解－好氧工艺处理后，好氧池出水的ＣＯＤｃｒ浓度为１６９．１ｍｇ／Ｌ，进一步混凝沉淀处理后，出水ＣＯＤｃｒ达８０ｍｇ／Ｌ。     

光催化氧化-混凝工艺处理化工废水

探索了光催化氧化－混凝工艺处理废水的工艺条件,最佳光催化氧化处理条件为ＰＨ＝３,催化剂为铁盐,氧化剂Ｈ２Ｏ２,低压汞灯,光照时间１．５ｈ,废水温度４５℃,温凝剂选用ＰＡＣ和ＰＡＭ（混凝剂的投加量为原水ＣＯＤｃｒ：ＰＡＣ：ＰＡＭ＝７：１．５：０．０１）,混凝ＰＨ６,沉降时间０．５ｈ,在该工艺条件对ＣＯＤｃｒ为１７３－７０１４４ｍｇ／Ｌ的十二烷基苯磺酸钠废水、苯酐废水、富马酸废水、邻苯二甲酸二辛酯废水     

The gas-photocatalytic degradation of trichloroethylene without water

The photocatalytic degradation of gaseous trichloroethylene (TCE) without water has been studied. The degradation products were determined to be CO₂, HCl and Cl₂, and the reaction stoichiometry, was described as

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. The degradation rate was found to be linear with 0.16 power of the illumination intensity. When the TCE concentration was low (10¹⁴ mol L⁻¹ or a little more), its degradation rate model could be considered as first order kinetics. A mechanism of valence band hole oxidation was proposed.     

Modeling biodegradation and kinetics of glyphosate by artificial neural network

An artificial neural network (ANN) model was developed to simulate the biodegradation of herbicide glyphosate [2-(Phosphonomethylamino) acetic acid] in a solution with varying parameters pH, inoculum size and initial glyphosate concentration. The predictive ability of ANN model was also compared with Monod model. The result showed that ANN model was able to accurately predict the experimental results. A low ratio of self-inhibition and half saturation constants of Haldane equations (< 8) exhibited the inhibitory effect of glyphosate on bacteria growth. The value of K(i)/K(s) increased when the mixed inoculum size was increased from 10(4) to 10(6) bacteria/mL. It was found that the percentage of glyphosate degradation reached a maximum value of 99% at an optimum pH 6-7 while for pH values higher than 9 or lower than 4, no degradation was observed.     

Loss of volatile hydrocarbons from an LNAPL oil source

The light nonaqueous phase liquid (LNAPL) oil pool in an aquifer that resulted from a pipeline spill near Bemidji, Minnesota, was analyzed for volatile hydrocarbons (VHCs) to determine if the composition of the oil remains constant over time. Oil samples were obtained from wells at five locations in the oil pool in an anaerobic part of the glacial outwash aquifer. Samples covering a 21-year period were analyzed for 25 VHCs. Compared to the composition of oil from the pipeline source, VHCs identified in oil from wells sampled in 2008 were 13 to 64% depleted. The magnitude of loss for the VHCs analyzed was toluene?o-xylene, benzene, C(6) and C(10-12)n-alkanes>C(7)-C(9)n-alkanes>m-xylene, cyclohexane, and 1- and 2-methylnaphthalene>1,2,4-trimethylbenzene and ethylbenzene. Other VHCs including p-xylene, 1,3,5- and 1,2,3-trimethylbenzenes, the tetramethylbenzenes, methyl- and ethyl-cyclohexane, and naphthalene were not depleted during the time of the study. Water-oil and air-water batch equilibration simulations indicate that volatilization and biodegradation is most important for the C(6)-C(9)n-alkanes and cyclohexanes; dissolution and biodegradation is important for most of the other hydrocarbons. Depletion of the hydrocarbons in the oil pool is controlled by: the lack of oxygen and nutrients, differing rates of recharge, and the spatial distribution of oil in the aquifer. The mass loss of these VHCs in the 5 wells is between 1.6 and 7.4% in 29years or an average annual loss of 0.06-0.26%/year. The present study shows that the composition of LNAPL changes over time and that these changes are spatially variable. This highlights the importance of characterizing the temporal and spatial variabilities of the source term in solute-transport models.     

Effect of arsenic-contaminated irrigation water on agricultural land soil and plants in West Bengal, India

Total arsenic withdrawn by the four shallow tubewells, used for agricultural irrigation in the arsenic-affected areas of Murshidabad district per year is 6.79 kg (mean: 1.79 kg, range: 0.56-3.53 kg) and the mean arsenic deposition on land per year is 5.02 kg ha(-1) (range: 2-9.81 kg ha(-1)). Mean soil arsenic concentrations in surface, root of plants, below ground level (0-30 cm) and all the soils, collected from four agricultural lands are 14.2 mg/kg (range: 9.5-19.4 mg/kg, n = 99), 13.7 mg/kg (range: 7.56-20.7 mg/kg, n = 99), 14.8 mg/kg (range: 8.69-21 mg/kg, n = 102) and 14.2 mg/kg (range: 7.56-21 mg/kg, n = 300) respectively. Higher the arsenic in groundwater, higher the arsenic in agricultural land soil and plants has been observed. Mean arsenic concentrations in root, stem, leaf and all parts of plants are 996 ng/g (range: <0.04-4850 ng/g, n = 99), 297 ng/g (range: <0.04-2900 ng/g, n = 99), 246 ng/g (range: <0.04-1600 ng/g, n = 99) and 513 ng/g (range: <0.04-4850 ng/g, n = 297) respectively. Approximately 3.1-13.1, 0.54-4.08 and 0.36-3.45% of arsenic is taken up by the root, stem and leaf respectively, from the soil.     

Adsorption and removal of As(V) and As(III) using Zr-loaded lysine diacetic acid chelating resin

An adsorption process for the removal of As(V) and As(III) was evaluated under various conditions using zirconium(IV) loaded chelating resin (Zr-LDA) with lysine-Nalpha,Nalpha diacetic acid functional groups. Arsenate ions strongly adsorbed in the pH range from 2 to 5, while arsenite was adsorbed between pH 7 and 10.5. The sorption mechanism is an additional complexation between arsenate or arsenite and Zr complex of LDA. Adsorption isotherm data could be well interpreted by Langmuir equation for As(V) at pH 4 and As(III) at pH 9 with a binding constant 227.93 and 270.47 dm3 mol(-1) and capacity constant 0.656 and 1.1843 mmol g(-1), respectively. Regeneration of the resin was carried out for As(V) using 1 M NaOH. Six adsorption/desorption cycles were performed without significant decrease in the uptake performance. Column adsorption studies showed that the adsorption of As(V) is more favorable compared to As(III), due to the faster kinetics of As(V) compared to As(III). Influence of the coexisting ions on the adsorption of As(V) and As(III) was studied. The applicability of the method for practical water samples was studied.     

Sequential treatment via Trametes versicolor and UV/TiO2/Ru(x)Se(y) to reduce contaminants in waste water resulting from the bleaching process during paper production

An efficient sequential, biological and photocatalytic treatment to reduce the pollutant levels in wastewater due to the bleaching process during paper production is reported. For a biological pre-treatment, 800 ml of non-sterilized effluent was inoculated with Trametes versicolor immobilized in polyurethane foam, with 25 g l(-1) glucose, 6.75 mM CuSO(4), and 0.22 mM MnSO(4) added, and cultured at 25 degrees C with an air flow of 800 ml min(-1) for 8d. The fungus did not inhibit growth of the heterotropic populations of the effluent. After 4d of culture, the chemical oxygen demand (COD) reduction and colour removal (CR) were 82% and 80%, respectively, with laccase (LAC) and manganese peroxidase (MnP) activities of 345 U l(-1) and 78 U l(-1), respectively. The COD reduction and CR correlated positively (p<0.0001) with LAC and MnP activities. Chlorophenol removal was 99% of pentachlorophenol, 99% of 2,3,4,6-tetrachlorophenol (2,3,4,6-TCP), 98% of 3,4-dichlorophenol (3,4-DCP) and 77% of 4-chlorophenol (4-CP), while 2,4,5-trichlorophenol (2,4,5-TCP) increased to 0.2 mg l(-1). The pre-treated effluent was then exposed to a photocatalytic treatment. The treatment with photolysis resulted in 9% CR and 46% COD reduction, 42% CR and 60% COD reduction by photocatalysis, and 62% CR and 85% COD reduction by heterogeneous photocatalysis with the system TiO(2)/Ru(x)Se(y) (Fig. 4). With this treatment the bacterial and fungal populations also decreased by 5 logarithmic units with respect to the biological treatment alone (Fig. 5). The total sequential treatment resulted in a 92% CR (from 5800 UC), 97% COD reduction (from 59 g l(-1)) and 99% chlorophenol removal at 96 h and 20 min.     

The mobile source effect on curbside 1,3-butadiene,benzene, and particle-bound polycyclic aromatic hydrocarbons assessed at a tollbooth

On-road mobile sources contribute substantially to ambient air concentrations of the carcinogens 1,3-butadiene, benzene, and polycyclic aromatic hydrocarbons (PAHs). The current study measured benzene and 1,3-butadiene at the Baltimore Harbor Tunnel tollbooth over 3-hr intervals on seven weekdays (n = 56). Particle-bound PAH was measured on a subset of three days. The 3-hr outdoor 1,3-butadiene levels varied according to time of day and traffic volume. The minimum occurred at night (12 a.m.-3 a.m.) with a mean of 2 microg/m3 (SD = 1.3, n = 7), while the maximum occurred during the morning rush hour (6 a.m.-9 a.m.) with a mean of 11.9 microg/m3 (SD = 4.6, n = 7). The corresponding traffic counts were 1413 (SD = 144) and 16,893 (SD = 692), respectively. During the same intervals, mean benzene concentration varied from 3 microg/m3 (SD = 3.1, n = 7) to 22.3 microg/m3 (SD = 7.6, n = 7). Median PAH concentrations ranged from 9 to 199 ng/m3. Using multivariate regression, a significant association (p < 0.001) between traffic and curbside concentration was observed. Much of the pollutant variability (1,3-butadiene 62%, benzene 77%, and PAH 85%) was explained by traffic volume, class, and meteorology. Results suggest > 2-axle vehicles emit 60, 32, and 9 times more PAH, 1,3-butadiene, and benzene, respectively, than do 2-axle vehicles. This study provides a model for estimating curbside pollution levels associated with traffic that may be relevant to exposures in the urban environment.     

Effects of DDT ground-spraying against tsetse flies on lizards in NW Zimbabwe

The impact of DDT ground-spraying against tsetse flies on lizards was investigated in NW Zimbabwe. Nineteen species were recorded, 17 in mopane woodland and 11 on gritstone outcrops: Mabuya striata wahlbergii dominated trees and Mabuya quinquetaeniata margaritifer rocks. Mean frequency of M. s. wahlbergii declined significantly from 76% of lizards at untreated sites (n = 8), through 72% after three annual treatments (n = 4), to 48% after 4-6 treatments (n = 6). Sighting rates and proportion of trees occupied were also significantly lower at treated than untreated sites. Numbers on trunks (99% > 15 cm diameter) above 3 m increased significantly with years of treatment relative to those in the spray target area below 3 m. Total DDT loads rose significantly with number of annual treatments and were up to 263 microg g(-1) lipid (7 microg g(-1) wet body weight) after 3-6 years. The percentage of unaltered DDT increased with load, which was proportionately higher in thin than in fat lizards. The geometric mean total DDT level in M. s. wahlbergii was significantly higher than in outcrop species, and from treated woodland was elevated 21 times above that in lizards from treated outcrops. Frequency and sighting rates of Lygodactylus chobiensis in woodland and immature Agama kirkii on outcrops were significantly higher in treated than in untreated areas.     

Bench-scale testing of selected remediation alternatives for contaminated sediments

The Assessment and Remediation of Contaminated Sediments (ARCS) Program within the U.S. Environmental Protection Agency's Great Lakes National Program Office (GLNPO) contained a component for demonstrating and evaluating sediment remediation technologies. Toward this end, bench-scale tests of solvent extraction, thermal desorption, and wet air oxidation technologies were conducted. Contaminated sediments were tested from the Grand Calumet River, Indiana; Buffalo River, New York; Saginaw River, Michigan; and Ashtabula River, Ohio. The primary contaminants of concern in these sediments were polychlorinated biphenyls (PCBs) and polynuclear aromatic hydrocarbons (PAHs). The solvent extraction tests were conducted with sediments from the Grand Calumet, Buffalo, and Saginaw rivers. The thermal desorption studies were conducted with sediments from the Grand Calumet, Buffalo, and Ashtabula rivers. The wet air oxidation testing was performed with the Grand Calumet River sediment. Raw sediment contaminant concentrations ranged from 0.32-21.9 mg/kg dry mass for PCBs and 2.70-266 mg/kg dry mass for PAHs. PCB removal or destruction efficiencies ranged from approximately 6-99%. PAH removal or destruction efficiencies ranged from 65-99%. Mass balance closures ranged from 40-99% for solids; 59-139% for water; 29-3500% for oil; 16-129% for PCBs; and 69-3170% for PAHs.