ZnOOH/O3催化臭氧化体系去除水中痕量对氯硝基苯

以实验室制备的羟基化锌（ZnOOH）为催化剂,考察了其催化臭氧化去除水中痕量对氯硝基苯（ppCNB能力.本实验条件下,蒸馏水中反应20　min时,催化臭氧化比单独臭氧化对pCNB的去除率提高了51 .3个百分点;催化过程遵循自由基反应机理,催化剂表面结合的羟基基团有利于催化反应;pCNB的去除效果随催化剂投量的增加而更佳,催化剂重复使用3次后,催化效果基本没有变化,水中的重碳酸盐以及缓冲溶液中的磷酸盐可以明显降低催化活性,中性条件下,催化作用最佳.     

你可别学他(双簧)

甲乙:今天我们哥儿俩为大家表演一段双簧. 乙:我先给这位兄弟化化妆.(边化边说) 人不打扮不好看,这要打扮好了您再看.(露出甲的脸) 甲:双簧是一种传统艺术,一个人在前面演,一个人在后面说.后面怎么说,前面就要怎么演.     

强化厌氧污泥体系同步脱硫反硝化特性研究

以硫化物为电子给体的自养反硝化厌氧体系是代替传统异养反硝化工艺处理低C/N比含氮废水的有效工艺,可以同时去除硫化物和硝酸盐.将脱氮硫杆菌菌悬液接种到厌氧污泥体系中,脱氮硫杆菌快速富集,采用5组进水比N/S比不同的反应瓶进行试验,运行15d后,测定不同时段的出水硫化物、硝酸盐、亚硝酸盐、硫酸盐浓度等指标,考察强化厌氧污泥体系去除硫化物和硝酸盐的特性,并对生化反应机制进行初步研究.结果表明,强化厌氧污泥体系运行3h后,进水中90%的硫化物被去除,硫化物的去除与进水N/S比无关,硫化物(以S计)去除速率高达20～24g·(m3·h)-1,是相关文献报道的10倍左右;运行6h后,进水中65%的硝氮被去除,硝氮的去除负荷随着进水N/S比的提高而增大,最高达到940g·(m3·h)-1,约为硫自养反硝化体系硝氮去除负荷的2倍,此时体系中亚硝氮积累,最高浓度达到93mg·L-1,进水N/S比低的条件下,6h后亚硝氮消失,进水N/S比较高时,21h后出水中未检测到亚硝氮.表明强化厌氧污泥体系停留6h后可以实现同时去除硫化物和硝酸盐,但硝酸盐首先转化为亚硝氮.与以往不同的是研究发现硫化物与生物硫粒产生多硫化合物的链式反应,是硫化物迅速转化的主要途径,此外,还原硝氮的电子给体并不来源于硫化物,可能主要来源于体系中产生的单质硫.     

镉对长江华溪蟹金属硫蛋白mRNA表达的诱导及低分子量壳聚糖的联合作用

采用实时荧光定量PCR法,研究了不同浓度镉（Cd2＋）对长江华溪蟹（Sinopotamon yangtsekiense）金属硫蛋白（metallothionein,简称MT）在肝胰腺、鳃、肌肉和心脏中mRNA表达的诱导作用及低分子量壳聚糖（lowmolecular weight chitosan,简称LMWC）的联合作...     

枯草芽孢杆菌对微污染水体的净化作用

采用投加枯草芽孢杆菌的水质净化方法,系统考察了在典型南方夏季气温下,封闭的模拟微污染水枯草芽孢杆菌净化体系中,投菌浓度、主要环境条件（pH和溶解氧）及其冲击对净化效果的影响.结果表明,枯草芽孢杆菌的最佳投菌浓度为3.2×105cfu·mL-1,适宜的环境条件为：pH5～7,溶解氧4～6mg·L-1.投菌9d后,CODM...     

荧光桃红-溴化十六烷基三甲基铵检测有机磷农药残留总量

在pH为6.40的B-R缓冲溶液中,荧光桃红与一定浓度的溴化十六烷基三甲基胺发生荧光增强反应,加入有机磷农药后,体系的荧光强度降低,且降低程度与有机磷农药的加入量呈良好的线性关系,建立了用此荧光法来测定有机磷农药残留总量的新方法.在优化试验条件下,线性范围为0.008-0.72 mg·L-1,检出限为0.05 mg·L...     

提高生产过程安全联锁系统可靠性的实用技术

以聚醚车间雾化器的安全联锁和工业蒸汽锅炉汽包的安全联锁两个实例,介绍了在安全性要求比较高的中、小型生产装置中,以较少的投资提高安全联锁系统可靠性的实用方法.这种基于冗余技术思想的实用安全技术,适用于石油化工生产过程及其它一些生产领域.     

Removal of phosphate by Fe-coordinated amino-functionalized 3D mesoporous silicates hybrid materials

Phosphate removal from aqueous waste streams is an important approach to control the eutrophication downstream bodies of water. A Fe(III) coordinated amino-functionalized silicate adsorbent for phosphate adsorption was synthesized by a post-grafting and metal cation incorporation process. The surface structure of the adsorbent was characterized by X-ray di raction, N2 adsoropion/desoprotion technique, and Fourier transform infrared spectroscopy. The experimental results showed that the adsorption equilibrium data were well fitted to the Langmuir equation. The maximum adsorption capacity of the modified silicate material was 51.8 mg/g. The kinetic data from the adsorption of phosphate were fitted to pseudo second-order model. The phosphate adsorption was highly pH dependent and the relatively high removal of phosphate fell within the pH range 3.0–6.0. The coexistence of other anions in solutions has an adverse e ect on phosphate adsorption; a decrease in adsorption capacity followed the order of exogenous anions: F?? > SO2?? 4 > NO??3 > Cl??. In addition, the adsorbed phosphate could be desorbed by NaOH solutions. This silicate adsorbent with a large adsorption capacity and relatively high selectivity could be utilized for the removal of phosphate from aqueous waste streams or in aquatic environment.     

Carbonyl sulfide and dimethyl sulfide fluxes in an urban lawn and adjacent bare soil in Guangzhou, China

Carbonyl sulfide (COS) and dimethyl sulfide (DMS) fluxes from an urban Cynodon dactylon lawn and adjacent bare soil were measured during April–July 2005 in Guangzhou, China. Both the lawn and bare soil acted as sinks for COS and sources for DMS. The mean fluxes of COS and DMS in the lawn (–19.27 and 18.16 pmol/(m2 sec), respectively) were significantly higher than those in the bare soil (–9.89 and 9.35 pmol/(m2 sec), respectively). Fluxes of COS and DMS in mowed lawn were also higher than those in bare soils. Both COS and DMS fluxes showed diurnal variation with detectable but much lower values in the nighttime than in the daytime. COS fluxes were related significantly to temperature and the optimal temperature for COS uptake was 29°C. While positive linear correlations were found between DMS fluxes and temperature. COS fluxes increased linearly with ambient COS mixing ratios, and had a compensation point of 336 ppt.     

Resistance and biosorption mechanism of silver ions by Bacillus cereus biomass

Biosorption of silver ions onto Bacillus cereus biomass was investigated. Overall kinetic experiments were performed for the determination of the necessary contact time for the attainment of equilibrium. It was found that the overall biosorption process was best described by pseudo second-order kinetic model. The crystals detected by scanning electron microscope and X-ray photoelectron spectroscopy suggested the precipitation was a possible mechanism of biosorption. The molecular genetics of silver resistance of B. cereus biomass was also detected and illustrated by a whole cell sensor tool.