Removal of Methyl Violet from aqueous solutions using poly （acrylic acid.co-acrylamide）/attapulgite composite

The adsorption of Methyl Violet (MV) cationic dye from aqueous solution was carried out by using crosslinked poly (acrylic acid-co-acrylamide)/attapulgite (Poly(AA-co-AM)/ATP) composite as adsorbent. The factors influencing adsorption capacity of the composite such as pH, concentration of the dye, temperature, contact time, adsorbent dosage, ionic strength and surfactant were systematically investigated. The equilibrium data fitted very well to the Langmuir isotherm and the maximum adsorption capacity reached 1194 mg/g at 30°C. The thermodynamic parameters including G0, △H0 and △S 0 for the adsorption processes of MV on the composite were also calculated, and the negative △H0 and △G0 confirmed that the adsorption process was exothermic and spontaneous. The kinetic studies showed that the adsorption process was consistent with the pseudo second-order kinetic model and the desorption studies revealed that the regeneration of the composite adsorbent can be easily achieved.     

采用双氰胺甲醛缩聚物混凝去除水中酸性红B染料的研究

以双氰胺和甲醛为原料制备了聚合双氰胺甲醛,并对其进行红外光谱表征.采用聚合双氰胺甲醛与硫代硫酸钠共同作用对酸性红B染料溶液进行混凝脱色实验.对比了单独使用聚合双氰胺甲醛,以及聚合双氰胺甲醛与硫代硫酸钠共同作用的脱色效果.探讨了硫代硫酸钠和聚合双氰胺甲醛的用量以及pH值对脱色率的影响.结果表明,投加硫代硫酸钠可以明显地提高聚合双氰胺甲醛的脱色率,增大絮凝范围,使絮凝剂对pH值的变化有很强的适应性,pH值为7～12的范围内,脱色率均能维持在96%以上.此外,还对混凝脱色的机理进行了研究.     

磁强化次氯酸钠氧化法处理邻硝基苯酚废水的实验研究

利用磁强化次氯酸钠氧化法对邻硝基苯酚废水进行了处理实验研究。结果表明,对于质量浓度为250mg／L、CODCr为2000mg／L、色度为150倍的100mL邻硝基苯酚废水,当次氯酸钠（2．5％）用量8mL、颗粒活性炭用量200mg、溶液pH为6．0、反应时间5min时,邻硝基苯酚的去除率达94．4％,CODCr的去除率达94．2％,色度的去除率达100％。采用外加磁场,当磁场强度为60mT时,邻硝基苯酚和CODCr达到相同的去除率,反应时间缩短了3min,显著提高了反应效率。同时对磁强化氧化法的机理进行了理论上的分析。     

Responses of antioxidant systems and LPO level to benzo(a)pyrene and benzo(k)fluoranthene in the haemolymph of the scallop Chlamys ferrari

The effects of benzo(a)pyrene (BaP), benzo(k)fluoranthene (BkF) and their mixture on antioxidant enzyme activities and lipid peroxidation (LPO) levels of haemolymph of scallop (Chlamys ferrari) were studied. The superoxide dismutase (SOD) activities of 0.5 microg/L and 1.0 microg/L were significantly higher than controls (P<0.05), while it increased at beginning and then dropped (lower than controls) in the end at 10.0 microg/L and 50.0 microg/L PAHs groups. The catalase (CAT) activities were very little during the whole experimental time. The glutathione peroxidase (GPx) activities in each PAHs group all increased significantly (P<0.05). LPO levels all increased significantly (P<0.05) with time at each PAHs group except for the 0.5 microg/L group of less than hour 12. The toxicity of PAHs in a descending order was BaP>BkF>mixture of BaP and BkF. The changes in antioxidant enzyme activities and LPO level in haemolymph could reflect the detoxification functions and damage levels of whole organism.     

污染土壤中苯并(a)芘的微生物降解

本文以B(a)P污染土壤为处理对象 ,进行了土壤微生物群体及单一菌对B(a)P的降解试验 ,结果表明 ,鲜土中的微生物降解力 >风干土的微生物降解力。土壤微生物群体比单一微生物降解B(a)P效果好。真菌的降解能力强于细菌。 2 2 0 9号镰刀菌降解B(a)P的速率最快 ,为高效降解菌     

海藻提取物EClean生物工程技术处理富营养型地表水

以北京动物园的地表水为例，利用引进的海藻提取物EClean生物工程技术对富营养化地表水进行处理试验研究。试验结果表明：应用此项技术有效降低了水体的浊度、COD和BOD5，水体脱氮降磷明显，藻类细胞密度下降，水体富营养化得到控制，减轻了“水华”藻类的危害。此技术在北京动物园富营养化水体的治理上表现出明显的应用效果。     

玉米粒为载体的流化床生物膜反应器处理印染废水

以废弃玉米粒为载体,在生物膜流化床试验装置上进行印染废水处理试验研究。结果表明,与炉渣载体比较成膜时间缩短2 d;形成的生物膜生长到载体内部,结合牢固;曝气量(20~30 L/h.L)受流化状况控制,比非生物质载体时略大,玉米粒含量为2~4 g/L时,COD、色度和浊度的去除率分别为72%、85%和86%。     

引滦河道中水质偏碱的起因研究

过分析揭示引滦河道pH值偏高的主要区域在于桥水库内,并分别从引滦河道流域内的岩石、土壤对地面水中溶质的影响、地下水运移及地面水中浮游植物的光合作用对水体pH值的影响等几方面寻找原因。经研究确定水体中藻类的光合作用是pH升高的主要原因。水中较高的氮、磷使藻类大量繁殖,而藻类在光合作用过程中,吸收二氧化碳,放出氧气,从而影响水中HCO-₃,CO₂和OH-的平衡,进而导致水体中pH升高。      

Experimental study and steady-state simulation of biogeochemical processes in laboratory columns with aquifer material

Packed bed laboratory column experiments were performed to simulate the biogeochemical processes resulting from microbially catalyzed oxidation of organic matter. These included aerobic respiration, denitrification, and Mn(IV), Fe(III) and SO(4) reduction processes. The effects of these reactions on the aqueous- and solid-phase geochemistry of the aquifer material were closely examined. The data were used to model the development of alkalinity and pH along the column. To study the independent development of Fe(III)- and SO(4)-reducing environments, two columns were used. One of the columns (column 1) contained small enough concentrations of SO(4) in the influent to render the reduction of this species unimportant to the geochemical processes in the column.The rate of microbially catalyzed reduction of Mn(IV) changed with time as evidenced by the variations in the initial rate of Mn(II) production at the head of the column. The concentration of Mn in both columns was controlled by the solubility of rhodochrosite (MnCO(3(S))).In the column where significant SO(4) reduction took place (column 2), the concentration of dissolved Fe(II) was controlled by the solubility of FeS. In column 1, where SO(4) reduction was not important, maximum dissolved Fe(II) concentrations were controlled by the solubility of siderite (FeCO(3(S))). Comparison of solid-phase and aqueous-phase data suggests that nearly 20% of the produced Fe(II) precipitates as siderite in column 1. The solid-phase analysis also indicates that during the course of experiment, approximately 20% of the total Fe(III) hydroxides and more than 70% of the amorphous Fe(III) hydroxides were reduced by dissimilatory iron reduction.The most important sink for dissolved S(-II) produced by the enzymatic reduction of SO(4) was its direct reaction with solid-phase Fe(III) hydroxides leading initially to the formation of FeS. Compared to this pathway, precipitation as FeS did not constitute an important sink for S(-II) in column 2. In this column, the total reacted S(-II) estimated from the concentration of dissolved sulfur species was in good agreement with the produced Cr(II)-reducible sulfur in the solid phase. Solid-phase analysis of the sulfur species indicated that up to half of the originally produced FeS may have possibly transformed to FeS(2).     

二氧化氯协同消毒在线自动控制系统的研究与应用

根据电解法制备二氧化氯混合消毒剂的工作原理和运行特性,采用单片机技术和余氯检测器,实现了对二氧化氯消毒设备的加盐、排碱及运行调节等全过程的在线自动控制,大大提高了二氧化氯发生量与投加量的控制精度,能耗盐耗明显降低,工作安全性和消毒效率显著提高,保证了饮用水质量的稳定性