铁山港海草生态区水体自净能力与水、生、化之间的关系

利用2008年1月～11月间对铁山港湾海草生态区进行的4个季节全面调查所获取的数据资料,首次探讨了该生态区水体自净能力与水动力特征及生物、化学因子之间的关系。结果表明:研究海区之所以具有较强的水体自净能力,其一与该海区具有强潮型的往复流水动力特征有关,在水体自净过程中起主导控制作用;其二与海区具有适宜的水温、快速的复氧能力、富足的溶解氧(DO)水平、最适合好氧微生物繁殖生长的环境条件有关,明显偏低的总有机碳(TOC)含量和丰富的总氮(TN)储量是有机物获得快速降解、营养盐获得快速再生、化学净化能力较强的重要体现;其三与生物链作用所体现的生化过程影响有关,DO含量与生物因子多呈显著以上负相关的季节变化特征以及三种形态N与生物因子在不同季节显示的相关性以事实佐证了这一点;而富足的TN储量、显著偏低的溶解无机氮(DIN)含量与繁盛的浮游动植物生物量及丰富的生物多样性同时出现的特征,正是研究海区具有较强生物净化能力的综合体现。与化学净化能力相比,生物净化能力显示出更强的优势,具有海草生态区的水体自净特点。     

内循环活性炭生物流化床处理农药生产废水的试验研究

采用内循环活性炭生物流化床反应器处理某农药厂生产废水,通过试验研究了该反应器在室温条件下处理农药生产废水的性能.结果表明:当进水pH值控制在7.0～7.5、水力停留时间为6h、曝气量控制在使活性炭处于流化状态时,CODcr的去除率为50％,总氮的去除率为32.33％,同时可生化性明显提高,生物毒性有所降低.     

序批式移动床生物膜反应器富集反硝化聚磷菌及其在单污泥系统中的应用

本文介绍了在单污泥系统中选择和富集反硝化聚磷菌的国内外研究进展,对不同研究者提出的选择和富集反硝化聚磷菌的方法进行了分析和评价,并提出将反硝化聚磷菌与移动床生物膜反应器工艺结合起来,在序批式移动床生物膜反应器悬浮填料上选择和富集反硝化聚磷菌,进一步认识了反硝化聚磷菌的生化特征,使其成为反应器中优势菌群,以及该工艺今后的研究重点。     

电催化氧化法处理阳离子染料废水的试验研究

以结晶紫作为阳离子染料,采用电催化氧化法对阳离子染料溶液进行了电解脱色处理试验,研究了电流密度、电解质种类、电解质浓度、pH值等对该溶液脱色率的影响,测定了电解时溶液中生成的余氯浓度和溶液的紫外-可见吸收光谱曲线,并对不同电解时间的溶液的吸光度进行了归一化计算。结果表明:随着电解时间的延长,水溶液中活性氯浓度不断上升,经一定时间后达到最大值;在电催化和活性氯的协同作用下,阳离子染料结晶紫分子中的大π共轭体系被破坏、苯环结构基本瓦解,溶液快速脱色;在电流密度为5.1mA/cm2、NaCl浓度为4g/L、pH值为9.41的条件下,初始浓度为100mg/L的结晶紫溶液经过20min的电解,其脱色率可高达98.31%。     

Transformations of particles, metal elements and natural organic matter in different water treatment processes

Characterizing natural organic matter （NOM）, particles and elements in different water treatment processes can give a useful information to optimize water treatment operations. In this article, transformations of particles, metal elements and NOM in a pilot-scale water treatment plant were investigated by laser light granularity system, particle counter, glass-fiber membrane filtration, inductively coupled plasma-optical emission spectroscopy, ultra filtration and resin absorbents fractionation. The results showed that particles, NOM and trihalomethane formation precursors were removed synergistically by sequential treatment of different processes. Preozonation markedly changed the polarity and molecular weight of NOM, and it could be conducive to the following coagulation process through destabilizing particles and colloids; mid-ozonation enhanced the subsequent granular activated carbon （GAC） filtration process by decreasing molecular weight of organic matters. Coagulation-flotation and GAC were more efficient in removing fixed suspended solids and larger particles; while sand-filtration was more efficient in removing volatile suspended solids and smaller particles. Flotation performed better than sedimentation in terms of particle and NOM removal. The type of coagulant could greatly affect the performance of coagulation-flotation. Pre-hydrolyzed composite coagulant （HPAC） was superior to FeCl3 concerning the removals of hydrophobic dissolved organic carbon and volatile suspended solids. The leakages of flocs from sand-filtration and microorganisms from GAC should be mitigated to ensure the reliability of the whole treatment system.     

Emissions of SO2, NO and N2O in a circulating fluidized bed combustor during co-firing coal and biomass

This paper presents the experimental investigations of the emissions of SO2, NO and N2O in a bench scale circulating fluidized bed combustor for coal combustion and co-firing coal and biomass. The thermal capacity of the combustor is 30 kW. The setup is electrically heated during startup. The influence of the excess air, the degree of the air staging, the biomass share and the feeding position of the fuels on the emissions of SO2, NO and N2O were studied. The results showed that an increase in the biomass shares resulted in an increase of the CO concentration in the flue gas, probably due to the high volatile content of the biomass. In co-firing, the emission of SO2 increased with increasing biomass share slightly, however, non-linear increase relationship between SO2 emission and fuel sulfur content was observed. Air staging significantly decreased the NO emission without raising the SO2 level. Although the change of the fuel feeding position from riser to downer resulted in a decrease in the NO emission level, no obvious change was observed for the SO2 level. Taking the coal feeding position R as a reference, the relative NO emission could significantly decrease during co-firing coal and biomass when feeding fuel at position D and keeping the first stage stoichiometry greater than 0.95. The possible mechanisms of the sulfur and nitrogen chemistry at these conditions were discussed and the ways of simultaneous reduction of SO2, NO and N2O were proposed.     

利用DGT高分辨率研究沉积物孔隙水中重金属的浓度和释放通量

2006年5月采集了大辽河河段3个柱状沉积物,测定了沉积物的理化性质和重金属元素的含量,并利用常规离心方法和DGT方法测定了柱状沉积物孔隙水中重金属元素的含量.研究发现沉积物中Cd、Co、Cr和Cu元素含量高低的顺序依次是Cr>Cu>Co>Cd.用DGT方法测定的孔隙水中Cd、Co、Cr和Cu的浓度比用离心方法测定的浓度要低.DGT测定的孔隙水中Cd、Co、Cr和Cu的浓度c_DGT与离心方法测定的孔隙水浓度c的平均比值R分别为0.389、0.328、0.863和0.403,这说明沉积物中这几种金属从固相到液相的再补给速率大小遵循如下规律：Cr>Cu>Cd>Co.沉积物中Cd、Co、Cr和Cu元素的释放通量分别为1.12×１０^{-7～3.28×10-7　nmol/(cm2·s)、2.48×１０-7～10.40×10-7　nmol/(cm2·s)、8.80×１０-6～12.65×10-6 nmol/(cm2·s)和6.14×１０-6～13.93×10-6　nmol/(cm2·s).相关分析结果表明,Cd和Cu元素的迁移转化主要受有机质影响;而Cr元素的迁移转化除了受有机质影响外,还受铁锰氧化物影响比较显著;而Co元素可能受氧化还原电位影响较大.}     

Anaerobic tapered fluidized bed reactor for starch wastewater treatment and modeling using multilayer perceptron neural network

Anaerobic treatability of synthetic sago wastewater was investigated in a laboratory anaerobic tapered fluidized bed reactor(ATFBR) with a mesoporous granular activated carbon(GAC)as a support material.The experimental protocol was defined to examine the effect of the maximum organic loading rate(OLR),hydraulic retention time(HRT),the efficiency of the reactor and to report on its steady- state performance.The reactor was subjected to a steady-state operation over a range of OLR up to 85.44 kg COD/(m~3.d).The COD removal efficiency was found to be 92% in the reactor while the biogas produced in the digester reached 25.38 m~3/(m~3·d) of the reactor. With the increase of OLR from 83.7 kg COD/(m~3.d),the COD removal efficiency decreased.Also an artificial neural network(ANN) model using multilayer perceptron(MLP)has been developed for a system of two input variable and five output dependent variables. For the training of the input-output data,the experimental values obtained have been used.The output parameters predicted have been found to be much closer to the corresponding experimental ones and the model was validated for 30% of the untrained data.The mean square error(MSE)was found to be only 0.0146.     

2008年南黄海西部浒苔暴发区有机碳的分布特征及浮游植物的固碳强度

根据2008-08-09～2008-08-13在南黄海西部绿潮(浒苔)暴发区取得的溶解有机碳(DOC)、颗粒有机碳(POC)和颗粒氮(PN)的分析数据,结合同步获得的水文环境要素资料,研究了该区域有机碳的分布特征、来源、影响因素以及浮游植物的固碳强度.结果表明,DOC的浓度范围为1.55～3.22mg/L,平均值为2.44mg/L;POC的浓度范围为0.11～0.68mg/L,平均值为0.27mg/L.DOC与POC的分布特征基本一致,呈现近岸高,外海低;表层高,底层低的趋势.POC与TSS的相关分析表明,POC与TSS整体上呈显著正相关,表明TSS的浓度和来源是控制POC浓度高低的重要因素.通过建立POC与PN的一元线性回归模型,估算了样品中PIN的含量.扣除样品中PIN的影响后,沿岸大部分海域POC/PON的平均值8,结合POC/Chl-a比值,表明沿岸海域POC主要是海洋有机质来源,并且存在降解有机物,这可能是调查期间处于绿潮暴发后期,部分浒苔开始腐烂被降解所致.应用初级生产力估算的浮游植物固碳强度的结果表明,南黄海西部绿潮(浒苔)暴发区浮游植物的固碳强度变化范围为167～2017mg/(m2·d),平均为730mg/(m2·d),该区域日固碳量达到2.95×104t.换算至整个黄海,日固碳量为28.03×104t.     

基于CFD的内构件强化内循环流化床流场结构分析

针对流化床内部流体结构的复杂性和缺乏有效放大设计理论的问题,以漏斗型导流内构件强化的内循环流化床的气液运动为研究对象,利用欧拉-欧拉双流体模型构建了能描述其复杂流动的CFD数学模型,通过宏观流场、气含率分布、液体速度分布解析内构件对气液混合传质的作用原理.数值模拟结果表明:双流体模型能较好地揭示流化床内气液流场结构,流...