Citrobacter sp. CK3对活性红KN-3B的脱色反应动力学研究

采用脱色菌Citrobacter sp. CK3,以活性红KN-3B染料为处理对象,在厌氧批式反应条件下,系统考察了pH值,温度和染料浓度对脱色反应速度的影响;通过动力学模拟及反应过程中染料的UV-Vis扫描图分析,探讨了脱色反应机理。结果表明：Citrobacter sp. CK3对活性红KN-3B的脱色反应的适宜pH为7～9;脱色反应速度在温度为32℃时达到最大。染料初浓度从57 mg/L逐渐增大到458 mg/L时脱色率逐渐降低。脱色过程中染料的偶氮键发生断裂,脱色反应符合二级反应动力学。     

缺氧-好氧生物滤池中高效菌对活性红KN-3B的降解特性

为了研究高效脱色菌在缺氧好氧生物滤池（A/O biofilter）中对偶氮染料的降解特性,以活性红KN-3B（C.I. reactive red 180）为降解对象,缺氧生物滤池以火山碎石为填料,接种高效脱色菌CK3柯氏柠檬酸杆菌启动,好氧生物滤池以牡蛎壳为填料,接种污水处理厂活性污泥启动。试验考察了不同工况下缺氧-好氧生物滤池对色度和COD的去除效果,结果表明：生物滤池中微生物对偶氮染料活性红KN-3B的脱色和对COD降解的最适pH条件为弱酸性;缺氧滤池中高效菌对色度的去除需要外加碳源,且增加外加碳源有助于脱色率的提高;该高效菌为耐盐菌,当进水NaCl浓度达30 g/L时,色度去除率仍可达93%以上;当染料负荷达500 mg/L时,脱色率仍可达95%。通过紫外-可见扫描图谱分析初步推断CK-3柯氏柠檬酸杆菌对偶氮染料活性红KN-3B的脱色主要是生物降解作用。     

壳聚糖在固定化光合细菌处理染料活性艳红X-3B中的应用研究

采用海藻酸钠对光合细菌进行包埋,并在固定化过程中加入壳聚糖,研究添加了壳聚糖的固定化细胞在不同条件下对活性艳红X-3B的脱色效果及其降解动力学.实验结果表明,在厌氧条件下,X-3B的脱色效果较好;染料浓度在30～300 mg/L之间变化时,厌氧降解动力学方程均符合一级动力学方程;降解速率与染料初始浓度之间关系符合Michaelis-Menten方程,反应动力学参数Km=374.96 mg/L,Vmax=7.53 mg/L·h.振荡有利于脱色并使半衰期缩短;固定化小球可重复使用.     

剩余污泥催化剂的制备及其脱色性能

以焦化废水脱水污泥为载体、ZnCl2为活化剂和催化剂的活性组分,采用一步法制备污泥催化剂。实验结果表明,当ZnCl2浓度为4 mol/L、固液比1∶3、焙烧温度550℃、焙烧时间40 min时,制备的污泥催化剂对亚甲基蓝的脱色性能最佳。利用制备的催化剂对活性红X-3B、弱酸性艳红B、活性蓝X-BR溶液进行脱色处理,研究反应时间、染料浓度、溶液pH、催化剂投加量和H2O2用量对染料脱色性能的影响。最佳条件下,3种废水的脱色率分别达到90.7%、97.5%和94.4%。对脱色数据进行动力学模拟,结果表明,3种染料废水脱色反应分别符合二级动力学模型、一级动力学模型、二级动力学模型。     

漆酶对活性艳蓝染料废水脱色

用白腐真菌漆酶对活性艳蓝X-BR和活性艳蓝K-NR 2种活性染料进行脱色实验。研究了pH、温度、染料浓度和酶活力对脱色率的影响。结果表明,漆酶脱色的适宜条件为:反应温度45℃,pH 6～7,适宜染料浓度为50 mg/L,酶浓度5 U/mL,反应1 h两种染料脱色率可达到75%;通过正交实验确定2种染料的最佳脱色组合分别为:反应温度55℃、pH7、活性艳蓝X-BR浓度50 mg/L、酶浓度5 U/mL和反应温度55℃、pH 6、活性艳蓝K-NR浓度50 mg/L、酶浓度5 U/mL。在所得最优条件下反应1 h,活性艳蓝X-BR和活性艳蓝K-NR的脱色率分别为74.2%和78.6%;反应2 h,脱色率分别为78%和79.5%。     

还原铁粉/紫外光体系对活性艳红X-3B溶液的脱色

研究了在紫外杀菌灯（λmax=253．7nm,30W）照射下,添加还原铁粉的活性艳红X－3B水溶液的脱色作用。当pH=3．5,铁粉投加量为2．0g／L时,20mg／L活性艳红X－3B溶液在光照180min后的脱色率为79％。脱色为动力学零级反应。染料溶液的pH、铁粉投加量、活性艳红初始浓度对脱色有影响。初步探讨了脱色反应的机理。     

Fe(0)-EDTA-空气体系降解活性黑染料废水

利用Fe(0)-EDTA-空气(ZEA)体系处理活性黑模拟染料废水。考察了活性黑初始浓度、反应温度、EDTA浓度和溶液酸度对降解效果的影响,用紫外可见吸收光谱检测了染料的降解过程。结果表明,Fe(0)-EDTA混合物在室温常压下,能够活化空气中的氧分子,进而使染料快速降解,升高温度和增加溶液酸度均能提高降解率。在pH为5.35,活性黑初始浓度为25 mg/L,EDTA浓度为0.1 mmol/L,Fe粉用量0.20 g,温度25℃时,脱色率达到95.60%,符合1级反应动力学。     

偶氮染料脱色菌Lysinibacillus sp.FS1的脱色性能

从佛山某工业园印染废水处理厂曝气池中,经梯度驯化筛选出一株对多种染料具有较强脱色能力的菌株FS1,通过16S r DNA基因序列分析初步鉴定为Lysinibacillus sp.,研究了该菌株在不同营养条件(氮源、碳源、碳源浓度),不同培养条件(p H、温度、供氧条件),不同染料(甲基橙、亚甲基蓝、中性红、酸性红B)和染料浓度下的脱色性能。结果表明,该菌株的最佳脱色条件:温度30~40℃,p H 7~9,氯化铵1 g/L,葡萄糖2 g/L的厌氧条件下培养脱色效果最好,10 h时对酸性红B脱色率可达98.73%左右,且脱色过程符合一级反应动力学方程:-ln(At/A0)=0.0588t-0.0448。该菌株可降解多种染料,脱色率均随污染强度的升高先增大后减小,对高浓度染料和混合染料也表现出很好的脱色效果,是一株高效广谱的染料降解菌,具有处理印染废水的开发应用价值。     

染料废水的脱色研究

模拟中温(35℃左右)厌氧消化条件,以葡萄糖为共基质,对模拟染料废水的厌氧生物脱色进行了研究.结果表明对可溶性的活性染料处理效果,脱色率和COD去除率可分别达到90%和70%左右.特别是对红、紫、橙三色染料处理效果好,如活性红KD-8B、活性艳兰KGL、活性金黄MG、活性红紫KN-2R、活性艳橙KGN等.当染料浓度在1.0 g/L以下,都没有抑制;脱色在22 h就可达90%的脱色率;污泥负荷在2～4 g/L时,处理效果最佳.实验亦证实,在厌氧处理过程中,染料分子结构发生了明显的变化.     

漆酶对活性黑KN-B和直接大红染料的脱色性能

利用白腐真菌漆酶对活性黑KN-B和直接大红2种偶氮染料进行脱色实验。考察反应时间、加酶量、pH值、染料浓度、温度对脱色率的影响,研究了ABTS介体以及金属离子存在下的脱色效果,并分析了漆酶脱色的动力学性能以及其对偶氮染料的降解规律。结果表明,活性黑KN-B和直接大红脱色适宜条件为：反应时间为30 min,加酶量8 U/mL,pH=7,染料浓度分别为50 mg/L和80 mg/L,温度40~45℃。ABTS介体对酶促偶氮染料脱色没有明显促进作用。Fe²⁺对漆酶脱色有较强的抑制作用;Cu²⁺对漆酶催化活性黑KN-B促进作用较大,对直接大红影响较小。漆酶对2种染料的脱色反应符合米氏方程,其催化活性黑KN-B和直接大红染料的K_m值分别为114.81 mg/L,317.5 mg/L,v_max值分别为6.57 mg/（L·min）和26.0 mg/（L·min）。     

Biodegradation of insecticide carbofuran by Paracoccus sp. YM3

A bacterium (Paracoccus sp. YM3) capable of degrading carbofuran was isolated from carbofuran-contaminated sludge. The strain was shown to metabolize carbofuran (50 mg L^?1) to carbofuran-7-phenol in minimal salt medium within 6 days in which the pesticide was the only source of carbon. Carbofuran and its main metabolite were analyzed by high performance liquid chromatography (HPLC). The addition of an other carbon source led to accelerated biodegradation. The relevant degrading-enzyme was intracellular and inducible. A tobacco hypersensitivity experiment showed that YM3 could eliminate carbofuran in soils effectively and safely. This is the first report of a Paracoccus sp. that could degrade carbofuran. The present study may provide a basis for biotreatment of wastewaters and bioremediation of carbofuran-contaminated soils.     

Effect of in vitro administered 2,3,7,8-tetrachlorodibenzo-p-dioxin (TCDD) on DNA-binding activities of nuclear transcription factors in NIH-3T3 mouse fibroblasts

Abstract

Most modern pesticides are expensive. Application of excessive dosage rates is likely to cause undesirable biological side‐effects and is economically wasteful. Non‐uniform distribution of the spray cloud, or application at the wrong time, may result in failure to control the pest. It is the responsibility of the field operator to acquire sufficient knowledge and skill to ensure proper use of the control agents, to increase efficiency of their usage and to reduce unwanted side‐effects. To achieve this goal, he must take into consideration the various physical factors that govern field performance of pesticides.

A simple relationship exists between the spray volume and emission rate used, and droplet size produced. The use of extremely low spray volumes (i.e., those less than 2.0 litre per ha) for forest insect control in Canada, as opposed to higher volumes used in agriculture, necessitates the release of fine droplets (ranging from 20 to 70 μm in diameter) to obtain adequate coverage of the target area. These droplets take a long time to sediment downwards, evaporate in‐flight, become smaller in size and/or form powdery residues, thus contributing to off‐target drift and impaired droplet adhesion to target surfaces. Physical factors such as rain washing, degradation by sunlight and erosion by wind also influence the longevity of pesticide deposits on foliage which is crucial during the critical period of pest control.

Factors affecting the mode of entry into insects are related to the type of ingredients used in formulation. If a pesticide acts via crawling contact, formulations which would provide surface deposits would be more beneficial than emulsions or oil‐based mixes which tend to undergo penetration into foliar cuticle. Physical factors that affect field performance of a pesticide tank mix are related to phase separation and ‘breakdown of emulsions’ in the application equipment; ‘agglomeration and caking’ of wettable powder dispersions at the bottom of the tank; impaired flow behaviour of highly viscous formulations; and coarse atomization of high‐viscosity tank mixes leading to poor target cover.     

Biodegradation of imidacloprid in liquid media by an isolated wastewater fungus Aspergillus terreus YESM3

In the present study, a new fungal strain capable of imidacloprid degradation was isolated from agricultural wastewater drain. The fungal strain of YESM3 was identified as Aspergillus terreus based on ITS1-5.8S rDNA-ITS2 gene sequence by PCR amplification of a 500 bp sequence. Screening of A. terreus YESM3 to the insecticide imidacloprid tolerance was achieved by growing fungus in Czapek Dox agar for 6 days at 28°C. High values (1.13 and 0.94 cm cm^?1) of tolerance index (TI) were recorded at 25 and 50 mg L^?1 of imidacloprid, respectively in the presence and absence of sucrose. However, at 400 mg L^?1 the fungus did not grow. Effects of the imidacloprid concentration, pH, and inoculum size on the biodegradation percentage were tested using Box–Behnken statistical design and the biodegradation was monitored by HPLC analysis at different time intervals. Box–Behnken results indicated that optimal conditions for biodegradation were at pH 4 and two fungal discs (10 mm diameter) in the presence of 61.2 mg L^?1 of imidacloprid. A. terreus YESM3 strain was capable of degrading 85% of imidacloprid 25 mg L^?1 in Czapek Dox broth medium at pH 4 and 28°C for 6 days under static conditions. In addition, after 20 days of inoculation, biodegradation recorded 96.23% of 25 mg L^?1 imidacloprid. Degradation kinetics showed that the imidacloprid followed the first order kinetics with half-life (t₅₀) of 1.532 day. Intermediate product identified as 6-chloronicotinic acid (6CNA) as one of the major metabolites during degradation of imidacloprid by using HPLC. Thus, A. terreus YESM3 showed a potential to reduce pollution by pesticides and toxicity in the effected environment. However, further studies should be conducted to understand the biodegradation mechanism of this pesticide in liquid media.     

Study of oil-water partitioning of a chemical dispersant using an acute bioassay with marine crustaceans

The toxicity of seawater dispersions of a chemical dispersant to two marine crustaceans was investigated in the presence and absence of various quantities of a non-toxic mineral oil. From the results and a physical-chemical partitioning analysis, a limiting value of the oil-water partition coefficient of the toxic compounds is deduced suggesting that essentially all of the toxic compounds in the dispersant will partition into solution in water following dispersant application to an oil spill. This conclusion simplifies interpretation and prediction of the toxic effects of a dispersed oil spill.The combined bioassay-partitioning procedure may have applications to the study of the toxicity of other complex mixtures such as industrial effluents.     

Bacteria additives to the changes in gaseous mass transfer from stored swine manure

Abstract

A bacteria additives treatment experiment in assessing the changes in gaseous mass transfer from stored swine manure is presented. The experiment is tested for ammonia, methane, hydrogen sulfide, and carbon dioxide emission data sampled from pilot swine manure columns and analyzed by GC/MS. The result shows that bacteria additives slightly reduce the methane and carbon dioxide releases, while the same additives do not show any effect on the reduction of ammonia. The hydrogen sulfide contents of stored swine manure continued to be low. Gas concentrations emitted from treated and untreated stored swine manure were: 3.76 and 2.2 ppm for methane, 0.35 and 0.11 ppm for ammonia, and 1000 and 470 ppm for carbon dioxide, respectively. A simple model to estimate gas emission rates is also developed from the viewpoint of two‐film resistance theory. The average emission rates calculated from the model for methane, ammonia, and carbon dioxide are respectively: 0.01, 0.0005, and 13.98 g/min from untreated stored manure; while 0.07, 0.096, and 0.55 g/min from treated manure. The emission model also indicates that for most gaseous pollutants of environmental concern, liquid phase transfer coefficient controls the rate of volatile compounds emitted from stored swine manure and gas phase transfer coefficient has insignificant effect in the calculation of overall mass transfer coefficient.     

The health effects and ecological significance of chlorine residuals in water

During the past several years, chlorine residuals and chlorinated organic compounds in drinking waters and aquatic environments have become a significant topic of study for scientists concerned about the quality of life in aquatic ecosystems as well as general public health. The effects of direct toxicity and/or carcinogenicity to human and aquatic life are the focal points for this concern.The effects of chloramines and chlorinated organic compounds present in the water distribution system after chlorination treatments are reviewed. Also discussed are the effects of chlorinated discharges from municipal secondary treatment plants and power plants on human health and aquatic life. The toxic significance of environmental chemicals are described.     

离子液体R_3NANR_3的制备及其脱硫性能

以二元酸和短链叔胺为原料,合成了已二酸三乙胺盐离子液体———R3NANR3。对该离子液体进行SO2气体的循环吸收和解吸行为的研究。实验结果表明,R3NANR3离子液体能对SO2气体进行有效的化学吸收。该吸收过程分二步进行,以第一步吸收为主。室温下（20℃）该离子液体在3 h以内吸收速率较快,3 h后吸收速率减慢并逐渐达到平衡。R3NANR3离子液体与SO2气体饱和吸收量的物质的量之比为1.08。较高温度将导致SO2气体的解吸,在90℃时饱和吸收液能较充分地解吸,残留量为0.0010 mol/L。多次吸收和解吸测试表明,R3NANR3离子液体能实现对SO2气体的循环吸收和分离,将成为烟气中SO2气体的脱除和利用的重要循环吸收剂。     

Fate of sprayed formulated aminocarb in freshwater

Following simulated aerial spraying of Matacil^® in field and tank experiments, the concentration of aminocarb increased in the subsurface water for some hours: 22 h in the case of the field and 72 h for the tank. Thereafter, the concentration of Matacil^® declined exponentially in subsurface waters. The equation for this, A = 4.834 + 0.165 g ? 0.155T, can be used to predict the concentration of aminocarb in the lentic environment (A, μgL^?1), providing the application rate (g ha^?1) and time after application (T in h) are known.