生物脱氮与甲烷化耦合的EGSB-BAF工艺模拟

以活性污泥3号模型(ASM3)为平台,通过引入厌氧氨氧化和甲烷化过程、以2步硝化-反硝化取代1步硝化-反硝化过程以及区分硝酸盐和亚硝酸盐条件下的内源呼吸过程,建立了同时具有甲烷化、厌氧氨氧化和2步硝化反硝化功能的EGSB-BAF工艺模型.该模型包括5种微生物、28个生物过程,同时考虑了温度、pH值和抑制性物质对生物过程的影响.以实验室EGSB-BAF集成工艺的实验数据,结合灵敏度分析对部分模型参数进行了校核.采用校核后的模型对集成工艺EGSB段和BAF段出水的COD、NH4+-N、NO2--N和NO3--N浓度进行模拟,结果表明,EGSB段和BAF段的出水中COD、NH4+-N、NO2--N和NO3--N浓度的模拟值与实测值的误差在可接受范围内.表明模型能够描述工艺的主要生物反应过程,可以作为指导工艺研究、设计和运行优化的手段.     

基于SIMULINK的硝化反应动力学模型的仿真

利用MATLAB/SIMULINK对序批式生物膜反应器内的氨氧化细菌与亚硝酸盐氧化菌的生化反应进行仿真预测。模型的验证结果表明,适当的选择模型中的溶解氧浓度、碱度以及温度3种参数,SIMULINK仿真动力学模型能够比较准确地对氨氧化细菌与亚硝酸氧化细菌处理生活污水的过程进行仿真和预测.NH4+-N、NO2--N和NO3--N 3种基质仿真值的绝对平均误差最大为15.88,最小为1.13;NH4+-N、NO2--N和NO3--N的Nash.Suttcliffe模拟效率系数分别为99.36%、98.64%和99.25%;此外,还对SIMULINK仿真动力学模型中的溶解氧浓度、碱度以及温度进行了灵敏度分析,结果表明,温度的灵敏度最大、溶解氧次之、碱度灵敏度相对最小。     

生物沸石滤池处理富营养化水体的挂膜实验

采用上向流生物沸石滤池处理富营养化水体,考察了挂膜阶段(前30 d)滤池对浊度、COD和TP等的去除效果,重点研究了系统中各形态氮素(NH4+-N、NO2--N、NO3--N和TN)的变化情况。结果表明,对于富营养化水体,生物沸石滤池对浊度、COD和TP的去除率分别约为80%、30%和24%;出水NH4+-N始终保持在0.5 mg/L以下,去除率在90%以上;NO2--N出现峰值(4.98 mg/L,第9 d),第13 d后即一直低于进水值;实验后期出水NO3--N与进水NH4+-N变化趋势基本一致,表明硝化生物膜已成熟,原位再生可行;生物沸石床内可能存在同步硝化反硝化现象。出水NO2-N浓度低于进水可作为生物沸石挂膜成功的一个标志。     

晚期垃圾渗滤液的部分亚硝化

利用实验室小试SBR在(33±1)℃的条件下,通过动态调控溶氧浓度(DO)(2～7 mg/L)和水力停留时间(2～5 d),经过130 d的运行成功启动了晚期垃圾渗滤液(NH4+-N含量1 227～2 133 mg/L)的部分亚硝化,使出水NO2--N∶NH4+-N稳定维持在1∶1左右,为后续的厌氧氨氧化工艺创造了进水条件。利用实时荧光定量PCR研究启动过程中的特异微生物氨氧化细菌的含量变化表明,氨氧化细菌的含量与NO2--N的生成速率和出水NO2--N稳定性有着显著相关性。     

容积负荷对厌氧氨氧化反应器运行影响的研究

采用1套有效容积为3 L的厌氧复合床作为厌氧氨氧化反应器,用提高进水基质浓度和缩短反应器水力停留时间2种方式提高反应器的容积负荷,进而研究反应器最佳的进水浓度和水力停留时间。结果表明,在HRT为24 h的条件下,反应器最佳进水浓度NH4+-N与NO2--N在110 mg/L左右;通过调节HRT发现,当HRT大于8 h时,NH4+-N与NO2--N的去除率都在80%以上。     

ASBR厌氧氨氧化反应器的快速启动及脱氮原理分析

以城市生活污水为基本水质进行配水,采用ASBR研究了厌氧氨氧化反应器的快速启动过程及脱氮性能。实验条件如下:T为(35±1)℃、HRT为24 h、pH为7.2～7.5,进水NH4+-N、NO2--N浓度为40～160 mg/L,TN负荷为0.08～0.34 kg TN/(m3.d),按2∶1比例混合接种好氧短程硝化污泥和厌氧氨氧化污泥,经49 d运行成功启动厌氧氨氧化反应器,并实现稳定运行。实验结果表明:稳定运行期NH4+-N、NO2--N去除率分别达96%和98%;NH4+-N、NO2--N去除量与NO3--N生成量比值为1∶1.05∶0.29,较为接近理论值;成功启动的反应器出水pH高于进水;系统TN去除率平均值为79.7%;反应器内存在反硝化与厌氧氨氧化的协同作用,实现了部分COD去除;污泥由深棕色絮状变成红褐色颗粒状,经SEM扫描电镜观察污泥菌群种类单一,多为球状菌,有漏斗状缺口,具有典型氨氧化菌形态特征。     

厌氧流化床微生物燃料电池同步除碳脱氮产电性能影响因素

研究了厌氧流化床微生物燃料电池(AFB-MFC)除碳脱氮产电性能的影响因素。结果表明:(1)AFB-MFC对NH4+-N的去除不起作用。电压下降主要是由于进水有机基质浓度下降造成。(2)不添加NO3--N时,在满足AFB-MFC脱氮所需的电子供体条件下增加进水COD/TN有利于AFB-MFC产电。(3)3种无机氮共存下,AFB-MFC在进水有机碳与无机氮质量比(C/N)不低于1.37时,对COD、NO2--N和NO3--N具有理想的去除效果。AFB-MFB在一定进水C/N范围内(1.37～2.50),能得到稳定的输出电压及功率密度。(4)固定进水C/N时,AFB-MFC在高碳氮负荷下仍能得到较理想的NO2--N、NO3--N、COD去除效果,AFB-MFC对NH4+-N去除效果不明显;增加碳氮负荷,AFB-MFC输出电压及功率密度没有明显的改变。(5)有机基质浓度不变下,AFB-MFC中充足的电子供体可保证较高的NO3--N、COD去除率。AFB-MFC输出电压及功率密度随着时间延长而先增加至稳定值后下降。     

高氨氮废水的半硝化工艺影响因素

采用泳动床反应器对含高浓度氨氮的污泥脱滤液进行了半硝化反应影响因素研究。实验结果表明,半硝化工艺可以在较高负荷条件下运行,其出水NO2--N/NH4+-N比例稳定在1.1±0.05∶1,基本满足了厌氧氨氧化工艺的进水要求。此外,温度和溶解氧对工艺运行具有重要影响,控制适宜无机碳含量与NH4+-N比值、碱度与氨氮比值有利于半硝化工艺的进行。     

厌氧氨氧化耦合部分反硝化处理低浓度氨氮废水

通过接种厌氧氨氧化菌(Candidatus Brocadia)与部分反硝化菌(Thauera)形成厌氧氨氧化与部分反硝化耦合处理模拟城镇污水中的氨氮(NH_4~+-N)与硝氮(NO3--N),考察不同NO3--N/NH_4~+-N比对耦合系统脱氮性能的影响及最佳NO3--N/NH_4~+-N比下耦合系统的稳定性和脱氮的途径。结果表明:在COD/NO3--N为2.5、NH_4~+-N浓度为20~40 mg·L~(-1)的条件下,NO3--N/NH_4~+-N比在0.8~1.6的范围内均可实现部分反硝化与厌氧氨氧化协同脱氮,且当NO3--N/NH_4~+-N比为1.2时,耦合效果最佳,对应的NH_4~+-N、NO3--N及总氮(TN)去除率分别为92.85%、99.68%和96.42%;厌氧氨氧化菌在耦合系统中的活性稳定在(4.62±0.44)mg·(g·h)-1(以VSS计),且与反硝化菌存在协同竞争关系,进水NO3--N的84.3%由厌氧氨氧化途径去除,15.7%由异养反硝化途径去除。     

纳米铁系双金属-微生物体系去除地下水NO-3-N研究

采用不同液相还原法制备纳米Fe0、Fe/Ni和Fe/Cu粒子,将其与反硝化细菌混合应用于地下水NO3--N去除研究。考察3种体系对NO3--N去除速率的影响,并对其脱氮产物及RNA水平上纳米铁系双金属对反硝化细菌的毒性效应进行了分析和讨论。结果表明,9 d内纳米Fe0体系可完全将NO3--N去除,过程中伴随NO2--N先升高后降低的生成趋势,NH 4+-N生成52%;纳米Fe/Ni体系脱氮速率最快,6 d内可将NO 3--N完全去除,几乎未检测到NO 2--N的生成,而NH 4+-N的转化率高达69%;纳米Fe/Cu体系7 d内可将NO3--N去除完全,NH4+-N的生成率降低,仅39%,但是出现33%NO2--N积累。从反应前后反硝化细菌总RNA浓度变化看,3种纳米粒子对反硝化细菌的毒性大小为纳米Fe/Ni﹥纳米Fe/Cu﹥纳米Fe0。     

厌氧消化1号模型(ADMl)的发展及其应用

国际水协(IWA)于2002年正式推出了厌氧消化1号模型(ADM1),其主要目的是建立一个厌氧工艺建模和模拟的通用平台,促进厌氧处理工艺技术的发展.近年来,ADMI在许多方面得到扩展,如包含硫酸盐还原、硝酸盐还原、产气及其释放的扩展等,这使ADM1更趋于完善.ADM1与其他污水处理数学模型结合的应用以及在分布参数模型中的应用是当前该模型应用的主要方面.有机物发酵的复杂性以及数量众多的模型动力学参数和组分都极人限制了该模型的广泛应用.     

Studies on reactions of ozone with alkenes

In the last years, a continuous increase of the O3 concentration has been recorded in the lower atmospheric layers. Photochemical reactions with NO(x), CO and organic compounds are the main sources of O3 in the troposphere. In this work, an attempt was made to determine the impact of alkenes on the O3 concentration in the troposphere. A study on the gas-phase reactions of 03 with 1-hexene, 1-heptene and 1-nonene was made. The reactions were carried out at room temperature under atmospheric pressure. Ozone was formed by the ultraviolet radiation emitted by a mercury lamp, in order to simulate the atmospheric conditions. The changes with time in the concentration of O3, 1-alkenes and formed aldehydes were investigated. Qualitative and quantitative analyses were done by means of the gas chromatography and colorimetry. The following products were identified: pentanal from 1-hexene; hexanal from 1-heptene; oktanal from 1-nonene. For each of the reactions, HCHO was also determined as a product. The reaction rate constants were calculated and obtained in units of 10(-17) cm(-3) molecule(-1) s(-1): 1.94-0.99 for 1-hexene, 5.54-4.51 for 1-heptene and 1.54-0.76 for 1-nonene. Based on the results obtained, an explanation of O3 concentration variations in the planetary boundary layer can be given. Last year a considerable increase of O3 concentration on the roads of Western Europe was recorded. This increase could have resulted from the decrease of alkene concentration in the air due to common use of the catalytic converters in cars. The unsaturated hydrocarbons rapidly oxidize on the catalyst. In Eastern Europe, where the amount of cars equipped with catalytic converters is smaller than in Western Europe, the alkene content in the exhaust fumes results in a decrease of the O3 concentration in the troposphere.     

苯为共代谢基质的1,1-二氯乙烯的好氧生物降解研究

为了更好地去除地下水中常见的共同存在且难降解的有机物苯与1,1-二氯乙烯（DCE）,研究了从苯与DCE驯化的活性污泥中筛选获得的菌株DB-TS对苯与DCE的降解特性。当苯初始浓度相同时,随着DCE初始浓度的增加,苯的降解率不断减少;而DCE的去除率先增加后降低。苯的降解符合一级反应动力学;DCE的降解符合Monod动力...     

The silvering process of European eel (Anguilla anguilla) influences PAH metabolite concentrations in bile fluid: consequences for monitoring

The stock of the catadromous European eel (Anguilla anguilla L.) continues to decline and there is growing evidence that poor health status due to contaminants might be a key element in this decrease. Organic contaminants such as polycyclic aromatic hydrocarbons (PAHs) belong to the major threats to yellow eel in their growth habitat and their metabolites are detectable in the bile. Starting the silvering process eels undergo physiological and morphological changes including cessation of feeding and downstream migration back to their spawning grounds. Reduced feed intake results in a diminishment of bile production and induces accumulation of e.g. PAH-metabolites in bile. Therefore, the aim of the present study was to demonstrate the impact of silvering on biliary PAH metabolite concentrations and to utilize normalization procedures to overcome silvering related accumulation effects of PAH-metabolites in eel bile. We investigated the hydroxyl-metabolites of pyrene (1-OH Pyr) and phenantrene (1-OH Phen) in the bile of different maturation stages of eels (silvering index I-V) from nine German rivers. We detected increasing absolute PAH metabolite levels in bile during the silvering process. The highest rise could be observed at the transition from pre migration stage III to the migrating stage IV, suggesting the onset of cessation of feeding at this stage. A cessation bias in PAH metabolite measurement could be diminished by normalization of absolute values against bile pigments (A₃₈₀, biliverdin). In conclusion, we demonstrated the impact of silvering on PAH metabolite concentrations in eel bile and present suitable normalization procedures to overcome silvering related accumulation effects. Thus, for a future eel monitoring we recommend (1) to regularly monitor PAH metabolites in bile, (2) to determine silvering index of eel and (3) to normalize PAH metabolite values in bile based on maturation/silvering stages. The knowledge of the silvering stage is mandatory for an unbiased evaluation of PAH contamination of European eel towards an international harmonized eel monitoring program.     

Biotransformation of Metamitron by Human P450 Expressed in Transgenic Tobacco Cell Cultures

In the present investigation, the oxidative metabolism of ¹⁴C-labeled metamitron was examined in plant cell cultures of tobacco overexpressing human P450 enzymes CYP1A1 or CYP1A2; special interest was in the aromatic hydroxylation of the herbicide. The oxidative metabolites deaminometamitron (DAM) and 4-hydroxydeaminometamitron (4-HDAM) were found in the untransformed control culture as well as in the transgenic culture. The transgenic cultures, however, exhibited higher turnover rates after 48 h of incubation with 20 μg ¹⁴C-metamitron per assay (untransformed: 40%, CYP1A1: 80%, CYP1A2: 100%). Primary metabolite 4-HDAM was partially found in glucosylated form in the transgenic cultures. As minor oxidative metabolites, 6-hydroxyphenyl-3-methoxymethyl-1,2,4-triazine-5(4H)-one and 3-hydroxymethyl-6-phenyl-1,2,4-triazine-5(4H)-one were identified in the transgenic cultures by GC-MS, LC-MS. Additionally, it could be demonstrated that both foreign enzymes (CYP1A1, CYP1A2) also catalyzed the deamination of metamitron. In a large-scale study (up to 400 μ g per assay) with the transgenic culture expressing CYP1A2, the high efficiency of this P450 system toward metamitron was demonstrated: turnover of the xenobiotic was almost complete with 400 μ g. Since large portions of unglucosylated 4-H-DAM were found, the activity of foreign CYP1A2 apparently exceeded that of endogenous O-glucosyltransferases of the tobacco cell culture. We concluded that in comparison to the nontransformed cell culture, the extent of metabolism was considerably higher in the transgenic cultures. The transgenic cell cultures expressing human CYP1A1 or CYP1A2 are thus suitable tools for the production of large quantities of primary oxidized metabolites of metamitron.     

树脂吸附法处理氯霉素中间体DL-氨基物合成废水

研究了树脂吸附法处理氯霉素生产中产生的DL 1 对硝基苯基 2 氨基 1 ,3 丙二醇 (DL 氨基物 )碱解废水的工艺。结果表明 ,NG 1 0 0超高交联吸附树脂对废水中DL 氨基物具有较好的吸附性能。在试验条件下 ,废水CODCr为 72 0 0mg/L ,DL 氨基物含量为 2 86 5mg/L ,批处理 1 7BV时 ,平均出水CODCr降至 89 3mg/L ,CODCr去除率 >98% ;出水中DL 氨基物未检出 ,去除率近 1 0 0 %。树脂经稀酸脱附处理后 ,再生性能良好 ,高浓脱附液可直接回用于氯霉素生产酸性水解工艺中 ,使回收物得到有效利用     

稳健GM(1,1)模型及其预测应用

本文提出了稳健GM(1,1)灰色模型,并用该模型建立了山东省工业固体废物产生量数学模型,结果表明,稳健GM(1,1)模型比通常的GM(1,1)模型更具预测应用价值.