Effect of nutrient conditions on the toxicity of naphthalene to Chlorella pyrenoidosa

The toxicity of naphthalene to a freshwater microalga, Chlorella pyrenoidosa, and the subsequent recovery of algae from the damage were investigated under two nutrient conditions, either enriched with nitrogen (N) and phosphorus (P), or starved of N and P. Results showed that C. pyrenoidosa was more sensitive to naphthalene under N,P-enriched condition, and the inhibitory rate generally increased at first and then decreased gradually with the evaporation of naphthalene under both nutrient conditions. Enriched N, P reduced the inhibitory rate at initial naphthalene concentration of 5 and 10 mg/L, but enhanced it at 100 mg/L, at which more severe ultrastructure damages were found than those under N,P-starved condition. Observed damages included partly or totally disappearance of nucleolus, nuclear, and plasma membranes. According to the chlorophyll content and cell density measurements, C. pyrenoidosa could recover from naphthalene damage with initial concentrations 6 50 mg/L in 7 days under both nutrient conditions, while they could not recover if the initial concentration of naphthalene was at 100 mg/L. Under the N,P-starved condition, the inability of C. pyrenoidosa to recover from the naphthalene damage was consistent with the results of high inhibitory rate, low value of specific growth rate (SGR, 0.05 day??1), and the severe destruction of cell structure. However, under the N,P-enriched conditions, the observed lower inhibitory rate, higher value of SGR (0.55 day??1), and the intact cell structure of most cells suggested that algae could potentially recover from the naphthalene damage.     

Mobilities and leachabilities of heavy metals in sludge with humus soil

Chemical forms of Zn, Ni, Cu, and Pb in municipal sewage sludge were investigated by adding humus soil to sludge and by performing sequential extraction procedures. In the final sludge mixtures, Zn and Ni were mainly found in Fe/Mn oxide-bound (F3) and organic matter/sulfide-bound (F4) forms. For Zn, exchangeable (F1), carbonate-bound (F2), and F3 forms were transformed to F4 and residual forms (F5). For Ni, F1 and F2 forms were transformed to F1, F2, and F3 forms. Both Cu and Pb were strongly associated with the stable forms F4 and F5. For Cu, F2 and F3 forms were major contributors, while for Pb, F3 and F4 forms were major contributors to F5. Humus soil dosage and pH conditions in the sludge were strongly correlated with the forms of heavy metals. Five forms were used to evaluate metal mobilities in the initial and final sludge mixtures. The mobilities of the four heavy metals studied decreased after 28 days. The metal mobilities in the final sludge mixtures were ranked in the following order: Ni > Zn > Cu = Pb. Leaching tests showed that the mobilities of Zn and Ni in lower pH conditions (pH 4) were higher than those in higher pH conditions (pH 8).     

Decolorization of dye solutions with Ruditapes philippinarum conglutination mud and the isolated bacteria

Application of Ruditapes Philippinarum conglutination mud (RPM) for decolorizing synthetic dye solutions was studied. RPM showed good activity for decolorization of Methylene Blue, Crystal Violet, Malachite Green, and Ink Blue. The amount of the RPM had great effect on the decoloration rate of the dye solutions. However, the decoloration rate did not continue to increase when the amount of mud exceeded the optimum dose. The temperature of the dye solution had a remarkable effect on the decolorization rate of Ink Blue solution, but had little effect on the other three dye solutions. The initial pH of the dye solutions evidently affected the decolorization rate of Malachite Green solution, but had less effect on the other three. The decolorization rate of the dye solutions increased significantly with treatment time within 8 hr, but tended to be steady after 8 hr for Methylene Blue, Crystal Violet and Malachite Green solutions, and after 12 hr for Ink Blue solution. The decolorization efficiencies for the four dye solutions under the optimum conditions were all above 90%. Seventeen strains screened from RPM showed flocculation ability for kaolin clay suspension. Out of them, the flocculation rate of strain ZHT3-9 and strain ZHT4-13 were up to 88.14% and 86.01%, respectively. ZHT3-9 was studied, and its decolorization rate for Methylene Blue, Crystal Violet, and Malachite Green reached 90.02%, 89.21%, and 80.29%, respectively. By morphological, physiological and biochemical characteristics analysis and 16S rRNA sequencing, the strain ZHT3-9 was identified as Arthrobacter sp.     

上海市供水管网中异养菌生长水平及相关指标变化

以上海市某水厂实际供水管网为研究对象,对其管网水中异养菌生长水平和其它相关物理、化学指标的变化规律进行了检测分析.结果表明,在所研究供水管段中,悬浮水中所含细菌主要是以有机物为营养的异养菌;随着供水距离延长,悬浮水中BDOC逐渐增加,伴随异养菌数量和浊度呈增加趋势;在研究管段中,悬浮水中各形态氮的变化表明水中存在一定的亚硝化作用,而且亚硝酸盐含量同异养菌具有相同的升高变化趋势;管网水中总磷含量与异养菌数量也随供水距离延长同时增加.     

石油化工企业有限空间中的气体检测

介绍了便携式气体检测报警仪用于石油化工企业中有限空间的气体检测时的采样方法、检测点选择、检测工作程序以及检测结果的处理.     

水质模型参数识别与验证的探讨

参数识别与模型验证是水质模型应用的两个重要步骤。在对模型参数的本质含义进行辨析的基础上,对模型参数的时变性、集成性和可识别性进行了分析。采用科学哲学的方法,对水质模型验证的必要性和不足进行了讨论,指出虽然模型验证必不可少,但也不能证实模型本身就是实际物理和生化过程的反映,因此应充分地意识到“经过验证的”模型在预测中的风险。     

粒状电介质形态对介质阻挡放电特性的影响

选取自制高岭土颗粒和氧化铝颗粒作为介质阻挡放电的电介质,并将其作为板-板式气体放电填充床反应器的填充材料,通过对反应器放电特性的实验研究。研究了电场强度、李萨如图形、放电功率以及电流脉冲情况,初步探讨了粒状电介质阻挡放电机制。并从粒径、成分、排序三个角度进行了结果分析,进而总结这三方面因素对气体放电的影响规律。     

剩余污泥的水解与氮磷回收

传统污水好氧生物处理过程中产生大量剩余污泥,这些污泥有机质中富含大量的氮磷元素。随着剩余污泥的消化并最终处置,大量的氮磷资源被白白浪费。在污泥消化过程中有机态氮磷可以在水解类细菌的水解作用下最终以氨氮和磷酸盐的形式溶出。当水解液中氨氮和磷酸盐达到一定浓度时,投加镁盐并调节pH,生成鸟粪石沉淀。鸟粪石作为一种缓释肥具有良好的经济效益。从资源回收的角度看,对剩余污泥水解酸化阶段研究有利于实现剩余污泥中氮磷资源的有效回收。     

膨润土对Cu^2＋的吸附及其它金属离子对Cu^2＋的竞争吸附

膨润土对重金属铜的吸附随铜离子浓度的增加先快迭增长而后趋于缓慢最后达成平衡。饱和吸附量为34．10mg·g^-1。Langmuir方程、Freundlich方程和Temkin方程均能拟舍实验结果,但Temkin方程拟合为最佳。pH是影响膨润土对Cu^2＋吸附的主要因素。低pH值不利于膨润土对Cu^2＋的吸附。引入竞争离子,膨润土对Cu^2＋的吸附量明显降低。Ph^2＋、Cd^2＋、Ni^2＋对Cu^2＋的吸附产生不同程度的竞争作用,其竞争力为Pb^2＋〉Cd^2＋〉Ni^2＋。在竞争离子存在的情况下,Cu^2＋的吸附依然遵守等温吸附模型。饱和吸附量从34．10mg·g^-1下降到16．93mg·g^-1（Pb^2＋）、19．21mg·g^-1（Cd^2＋）、26．08mg·g^-1（Ni^2＋）。     

膜生物反应器内污泥增长规律的研究

研究了不同进水有机物浓度下MBR反应器的污泥增长和活性变化的规律,并确定了本系统三个运行阶段活性污泥增长的动力学系数（Yg和ms）。结果表明,MBR长时间不排泥和低负荷的运行方式会使污泥的活性下降和微生物种群的改变,在低负荷下运行时会出现污泥的负增长。根据经典的微生物能量代谢理论并结合各个运行阶段污泥浓度的变化情况计算得到进水COD300、180和120mg／L下MBR的Yg和ms的值,分别为0．42、0．39、0．24（gVSSgCOD^-1）和0．11、0．06、0．08（gCODgVSS^-1day^-1）。