SO2和O3动态胁迫烟草致病的暴露试验

ＳＯ_２和Ｏ_３动态胁迫烟草致病的暴露试验陈锦云，兰志斌，苏珍山，曾军，王阳青（福建龙岩地区烟科所龙岩３６４０００）关键词Ｓ）_２和Ｏ_３；烟草；气候斑点病，动态胁迫暴露ＴＨＥＤＹＮＡＭＩＣＳＴＲＥＳＳＥＸＰＯＳＵＲＥＴＥＳＴＯＮＴＯＢＡＣＣＯＢＬＡＤＥ...     

Al13形态分离纯化方法的初步研究

对ＳＯ＾２－４／Ｂａ＾２＋法分离提纯Ａｌ１３形态的影响因素进行了研究,实验结果表明,聚合铝浓度、ＳＯ４／Ａｌ比、Ｂａ／ＳＯ４摩尔比、以及超声反应时间对分离效果上具有较大的影响。较高浓度的聚合铝利于沉淀的形成与分离。同时选用１：１的ＳＯ４／Ａｌ与Ｂａ＾２＋的共存对形态分析不产生影响,形态鉴定结果表明,经过上述分离条件所得产物形态为Ａｌ１３。     

PACS的结构特征及絮凝性能研究

制备了碱化度及Ａｌ＾３＋／ＳＯ＾２－４摩尔比不同的系列ＰＡＣＳ，分别进行常压（干燥温度１０５℃）及真空干燥（真空度为－０．０９８ＭＰａ、干燥温度６５℃）制备固体产品。用红外光谱及Ｘ－射线衍射谱研究了碱化度、Ａｌ＾３＋／ＳＯ＾２－４摩尔比、干燥温度对ＰＡＣＳ的结构影响，比较了干燥温度不同对ＰＡＣＳ固体样品的溶解度及絮凝效果的影响，借助于显微电泳测定技术研究不同碱化度及不同Ａｌ＾３＋／ＳＯ＾２－４摩尔     

磷和硫对空心菜吸收砷的影响

本文通过水培空心菜中砷与磷以及砷与硫配比试验，研究了ＰＯ＾３－４和ＡｓＯ＾３－４以及ＳＯ＾２－４和ＡｓＯ３＾３－４共存对空心菜生长及砷累积的影响。结果表明：５ｍｇ．ｌ＾－１ＰＯ＾３－４或ＳＯ＾２－４时，ＡｓＯ＾３－４显著降低空心菜产量，ＰＯ＾３－４和ＳＯ＾２－４含量提高到３０－１００ｍｇ．ｌ＾－１时，空心菜产量明显提高。．     

Al—Ferron逐时络合比色法研究PACS中铝的水解聚合形态

制备了碱化度及不同Ａｌ＾３＋／ＳＯ＾２＝４摩尔比的系列ＰＡＣＳ，用Ａｌ－Ｆｅｒｒｏｎ逐时络合比色法研究了铝的形态分布，考察了碱化度，Ａｌ＾３＝／ＳＯ＾２＝４摩尔比，稀释作用及ｐＨ值对铝的形态分布的影响。     

有机磷农药敏作用的初步研究

本文研究了有机磷农药甲基１６０５和毒死蜱对＾１Ｏ２探针性物质二乙基二硫醚，萜品烯及ＲＯＯ和ＲＯ探针性物质２，６－二叔丁基－４－甲基苯酚和１，２，３，４－四氢萘光降解的敏化作用。结果表明基态氧直接参与了ＤＥＳ和α－ｔｅｒｐ的光解；在甲基１６０５的作用下，１／Ｋｅｘｐｔｌ与「αｔｅｒｐ」的关系表明，α－ｔｅｒｐ的降解不为＾１Ｏ２历程。     

雨水中S（Ⅳ）的离子色谱分析及其保护方法的研究

本文研究了用离子色谱法分析雨水中Ｓ（Ⅳ）的色谱条件和含Ｓ（Ⅳ）样品的保存方法，采用ＨＰＩＣ＿ＡＳＡ分离柱、用２ｍｍｏｌ．ｌ＾－１Ｎａ２ＣＯ３／３ｍｍｏｌ．ｌ＾０１ＮａＯＨ溶液作淋洗液、０．０１２５ｍｏｌ．ｌ＾－１Ｈ２ＳＯ４为再生液、电导检测的方法，具有无干扰和灵敏度高等优点，而且在Ｓ（Ⅵ）的浓度秋－２８μｇ．ｍｌ＾－１范围内，其浓度与响应值之间呈现出良好的线性关系，其线性相关系数在０．９９９５以上     

饮水的化学组分与地氟病的关系

饮水的化学成分分析结果表明，徐州地区居民饮用水中的氟含量ｐＨ，Ｎａ＾＋，ＨＣＯ＾－３，Ａｓ，Ｂ和矿化度呈正相关关系，与Ｋ＾＋，Ｃａ＾２＋，Ａｌ＾３＋，Ｂａ＾２＋，Ｓｉ＾４＋呈负相关关系。地氟病的发病率不仅与饮水的氟含量密切相关，而且受饮水中其它组份的制榴，饮水中Ｃａ＾２＋，Ａｌ＾３＋，Ｓｒ＾２＋，Ｂ，Ｓｉ＾４＋，Ｋ＾＋，Ｇｅ＾４＋等组分的增高可抑制或减缓地氟病的发生。     

循环式活性污泥法处理城市污水

循环式活性污泥法工艺（ＣＡＳＴ）是序批式活性污泥法工艺（ＳＢＲ）的一种变型。它综合活性污泥法和ＳＢＲ工艺特点,与生物选择器原理结合在一起,真有抗冲击负荷和除磷脱氮功能。本文介绍了该工艺的特点,以及处理城市污水的工程设计。     

Fe（Ⅲ）水解过程中无机阴离子的影响作用

本文通过ＰＯ＾３－ ４，Ｆ＾－，ＳＯ＾２－ ４，Ｃｌ＾－，ＮＯ＾－ ３和ＣｌＯ＾－ ４存在时，０．１ｍｏｌ／１ ＦｅＣｌ３溶液的碱中和曲线的分析对比，说明了用曲线斜率区分滴定曲线为三个区域：（Ａ）自发水解反应；（Ｂ）聚合反应；（Ｃ）沉淀反应，以及阴离子对中和曲线的影响及其规律，指出阴子子对Ｆｅ（Ⅲ）浓度中和反应影响为不同程度的竞争配位，参与聚合及电中和脱稳，使沉淀反应提前等。并与ＯＨ＾－共同形成Ｆ     

Practical consideration for design and optimization of the step feed process

Based on the anoxic/oxic (A/O) step feed process, a modified University of Cape Town (UCT) step feed process was developed by adding an anaerobic zone and adjusting sludge return pipeline. Performance evaluation of these two types of processes was investigated by optimizing operational parameters, such as the anaerobic/anoxic/oxic volumes, internal recycle ratios, and sludge retention times, for removal of chemical oxygen demanding (COD), nitrogen, and phosphorus. Results showed high removal efficiencies of COD of (85.0±1.7)%, ammonium of (99.7±0.2)%, total nitrogen (TN) of (85.5±1.7)%, phosphorus of (95.1±3.3)%, as well as excellent sludge settleability with average sludge volume index of (83.7±9.5) L·mg^-1 in the modified UCT process. Moreover, (61.5±6.0)% of influent COD was efficiently involved in denitrification or phosphorus release process. As much as 35.3% of TN was eliminated through simultaneous nitrification and denitrification process in aerobic zones. In addition, the presence of denitrifying phosphorus accumulating organisms (DNPAOs), accounting for approximately 39.2% of PAOs, was also greatly beneficial to the nitrogen and phosphorus removal. Consequently, the modified UCT step feed process was more attractive for the wastewater treatment plant, because it had extremely competitive advantages such as higher nutrient removal efficiencies, lower energy and dosages consumption, excellent settling sludge and operational assurance.     

A/O-MBR处理某经济区市政污水的效能

采用A/O-MBR法处理某经济区市政污水,对其进、出水的水质进行连续监测,考察系统稳定性和处理效果。结果表明,在水力停留时间12小时,污泥龄30天,回流比75%,好氧段DO浓度1.3～8.5 mg/L的条件下,系统对COD、氨氮、总氮、总磷的平均去除率分别为92.04%、93.66%、78.04%、91.06%。反硝化...     

Optimization of phosphorus removal in uniFed SBR system for domestic wastewater treatment

The characteristic of phosphorus removal and appropriate change of the traditional operation modes were investigated in UniFed sequencing batch reactor (SBR) laboratory-scale apparatus (40 L), treating actual domestic wastewater with low ratios of C/N (2.57) and C/P (30.18), providing theoretical basis for actual application of wastewater treatment plant. UniFed SBR system with its unique operation mode had the distinct superiority of phosphorus removal. On this occasion, the effect of volumetric exchange ratio (VER) and the method of influent introduction for phosphorus removal were studied. When the carbon source became the limiting factor to phosphorus release, the higher the VER, the lower the phosphorus concentration in the effluent. Three different influent patterns, including one-time filling, four-time filling, and continuous filling with the same quantity of wastewater could increase the release rate of anaerobic phosphorus from 0.082 to 0.143 mg·P·(L·min)^-1. Appropriate change of the traditional operation modes could optimize the efficiency of phosphorus removal. When the feed/ decant time was extended from 2 h to 4 h, the phosphorous removal efficiency increased from 59.93% to 88.45% without any external carbon source. In the mode of alternation of anoxic-aerobic (A/O) condition, phosphorous removal efficiency increased from 55.07% to 72.27% clearly. The carbon source in the influent can be used adequately, and denitrifying phosphorus removal was carried out in anoxic stage 2 (A2). This mode was optimal for the treatment of actual domestic wastewater with low C/N and C/P ratios.     

Simultaneous denitrifying phosphorus accumulation in a sequencing batch reactor

In order to achieve simultaneous nitrogen and phosphorus removal in the biological treatment process, denitrifying phosphorus accumulation (DNPA) and its affecting factors were studied in a sequencing batch reactor (SBR) with synthetic wastewater. The results showed that when acetate was used as the sole carbon resource in the influent, the sludge acclimatized under anaerobic/aerobic operation had good phosphorus removal ability. Denitrifying phosphorus accumulation was observed soon when fed with nitrate instead of aeration following the anaerobic stage, which is a vital premise to DNPA. If DNPA sludge is fed with nitrate prior to the anaerobic stage, the DNPA would weaken or even disappear. At the high concentration of nitrate fed in the anoxic stage, the longer anoxic time needed, the better the DNPA was. Induced DNPA did not disappear even though an aerobic stage followed the anoxic stage, but the shorter the aerobic stage lasted, the higher the proportions of phosphorus removal via DNPA to total removal.     

序批式生物膜法同步除磷脱氮特性研究

对淹没序批式生物膜法去除有机物和磷及同步部分脱氮的特性进行了研究。其适合的载体装填密度为30％，水力停留时间为9h，其中厌氧3h，好氧6h，进水COD负荷从0．27kg/(m^3.d)到1．32kg/(m^3.d)均可使除磷率达90％以上，脱氮率达50％－60％。淹没式生物膜法除磷脱氮工艺中的优势菌属为假单胞菌属，其次依顺序为气单胞菌属，芽孢杆菌属，微球菌属，硝化矸菌属，生物膜具有生物量大（MLVSS达5531．7mg/L)，脱落污泥含磷量高（达5．67％），沉降性好（SVI为101．7）的特点，污泥产率为0．1996kg干泥／kgCOD。     

两段式A/O-MBR工艺在方庄污水厂改造工程中的应用设计

为将北京市方庄污水处理厂处理出水的排放标准由一级B提升至一级A,需进行提标改造工程。在原有A/A/O＋生物填料的CNR工艺的基础上,采用两段式A/O-MBR工艺进行改造升级,强化脱氮除磷效果。预计该工艺对COD、NH3-N和SS的去除率可分别达到95.2%、98%和99.1%;对于氮磷的去除,出水TN〈9.0 mg/L,TP〈0.3 mg/L,各指标均可实现《城镇污水处理厂污染物排放标准》（GBl8918-2002）中一级A排放标准。     

废水生物脱氮中N_2O和NO_x的产生和作用

废水生物脱氮中N2O和NOx来源于硝化、反硝化、厌氧氨氧化和化学反硝化等过程.电子受体和供体浓度、pH、缓冲剂类型、有机负荷、微生物种类及其相互作用等都会影响这些气态中间产物的产生.NO2能够氧化氨和强化好氧和厌氧氨氧化,NO能够阻止C2H2对好氧氨氧化活性的抑制,两者对好氧氨氧化活性的恢复至关重要.所有这些表明,废水生物脱氮的气态中间产物N2O和NOx在氮的生物转化中具有重要的正面作用,甚至必不可少.基于NO2曝气技术和Brocadiaanammoxidans与Nitrosomonas协同作用的废水生物脱氮新技术开发是今后一段时间的重要研究方向.图4参35     

N2O emission from a sequencing batch reactor for biological N and P removal from wastewater

Nitrous oxide （N2O） is a greenhouse gas that can be released during biological nitrogen removal from wastewater. N2O emission from a sequencing batch reactor （SBR） for biological nitrogen and phosphorus removal from wastewater was investigated, and the aims were to examine which process, nitrification or denitrification, would contribute more to N2Oemission and to study the effects of heterotrophic activities on N2O emission during nitrification. The results showed that N2O emission was mainly attributed to nitrification rather than to denitrification. N2O emission during denitrification mainly occurred with stored organic carbon as the electron donor. During nitrification, NaO emission was increased with increasing initial ammonium or nitrite concentrations. The ratio of N2O emission to the removed ammonium nitrogen （N2O- N/NH4-N） was 2.5% in the SBR system with high heterotrophic activities, while this ratio was in the range from 0.14% to 1.06% in batch nitrification experiments with limited heterotrophic activities.     

Research on polyhydroxyalkanoates and glycogen transformations: Key aspects to biologic nitrogen and phosphorus removal in low dissolved oxygen systems

In this paper, a study was conducted on the effect of polyhydroxyalkanoates (PHA) and glycogen transformations on biologic nitrogen and phosphorus removal in low dissolved oxygen (DO) systems. Two laboratory-scale sequencing batch reactors (SBR1 and SBR2) were operating with anaerobic/aerobic (low DO, 0.15–0.45 mg·L^-1) configurations, which cultured a propionic to acetic acid ratio (molar carbon ratio) of 1.0 and 2.0, respectively. Fewer poly-3-hydroxybutyrate (PHB), total PHA, and glycogen transformations were observed with the increase of propionic/acetic acid, along with more poly-3-hydroxyvalerate (PHV) and poly-3-hydroxy-2-methyvalerate (PH2MV) shifts. The total nitrogen (TN) removal efficiency was 68% and 82% in SBR1 and SBR2, respectively. In the two SBRs, the soluble ortho-phosphate (SOP) removal efficiency was 94% and 99%, and the average sludge polyphosphate (poly-P) content (g·g-MLVSS^-1) was 8.3% and 10.2%, respectively. Thus, the propionic to acetic acid ratio of the influent greatly influenced the PHA form and quantity, glycogen transformation, and poly-P contained in activated sludge and further determined TN and SOP removal efficiency. Moreover, significant correlations between the SOP removal rate and the (PHV+ PH2MV)/PHA ratio were observed (R²>0.99). Accordingly, PHA and glycogen transformations should be taken into account as key components for optimizing anaerobic/aerobic (low DO) biologic nitrogen and phosphorus removal systems.     

Enhanced nutrients removal from municipal wastewater through biological phosphorus removal followed by partial nitritation/anammox

Conventional biological removal of nitrogen and phosphorus is usually limited due to the lack of biodegradable carbon source, therefore, new methods are needed. In this study, a new alternative consisting of enhanced biological phosphorus removal (EBPR) followed by partial nitritationanammox (PN/A), is proposed to enhance nutrients removal from municipal wastewater. Research was carried out in a laboratory-scale system of combined two sequencing batch reactors (SBRs). In SBR1, phosphorus removal was achieved under an alternating anaerobic-aerobic condition and ammonium concentration stayed the same since nitrifiers were washed out from the reactor under short sludge retention time of 2–3 d. The remaining ammonium was further treated in SBR2 where PN/A was established by inoculation. A maximum of nitrogen removal rate of 0.12 kg N?m^–3?d^–1 was finally achieved. During the stable period, effluent concentrations of total phosphorus and total nitrogen were 0.25 and 10.8 mg?L^–1, respectively. This study suggests EBPR-PN/A process is feasible to enhance nutrients removal from municipal wastewater of low influent carbon source.

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