中试厌氧氨氧化反应器的启动与调控

研究了中试厌氧氨氧化(Anaerobic ammonium oxidation,Anammox)反应器的启动性能。结果表明,以硝化反硝化污泥、短程硝化污泥、厌氧絮体污泥和厌氧颗粒污泥混合接种,经过255d的运行,可在常温下(5oC～27oC)成功启动中试Anammox反应器,反应器的基质氮去除速率可达1.30kg/(m3·d)。厌氧氨氧化是致碱反应,厌氧氨氧化成为反应器内的主导反应后,进水pH宜控制在厌氧氨氧化适宜范围的偏低水平(6.8左右)。亚硝酸盐既是Anammox菌的基质,也是抑制剂,控制进水亚硝酸盐浓度(13～36mg/L)有助于厌氧氨氧化反应。菌种是生物反应器的功能之源,向中试装置投加少量厌氧氨氧化污泥(投加比2%),可大大加速中试Anammox反应器的启动进程。     

固定载体卧式厌氧反应器处理糖蜜废水的快速启动

为高效处理高浓度有机废水而设计了固定载体卧式厌氧反应器R1和R2, 它是厌氧折流板反应器(ABR)的改进, 以活性炭纤维作为生物膜载体固定并充当反应器的折流板, 在实验室规模上对R1和R2处理糖蜜废水进行快速启动运行。HRT和ORL是影响R1和R2稳定高效运行及启动的2个重要工艺参数。实验证明: HRT为2 d时, 反应器运行最佳。在第30天时, R1的COD去除率达到84.88%, R2达到81.72%。随着进水ORL由1.25 kg/(m3·d)提升到10 kg/(m3·d), 沼气容积产气率由0.35 L/(L·d)逐渐增加到4.98 L/(L·d)。进水pH值为3.9?4.5之间, 整个启动运行过程中, 未调节pH值, R1和R2的出水pH值均在6.7?7.6之间, 2个反应器均有较强的抗酸能力, R1的pH波动更为平缓。在整个实验过程中, 污泥流失量小, 没有发生堵塞现象, 在处理酸性高浓度有机废水时, 2个反应器均表现出较强的抗负荷冲击能力。     

Anammox反应器启动过程中颗粒污泥性状变化特性

以厌氧颗粒污泥作为接种物,通过185 d的运行,成功启动了上流式厌氧氨氧化污泥床(Upflow anaerobic sludge blanket,UASB)反应器。反应器的进水氨氮与亚硝氮浓度分别提升至224 mg/L和255 mg/L,容积氮去除速率提升至3.76 kg/(m3·d)。采用红外光谱、扫描电镜和透射电镜等对厌氧氨氧化颗粒污泥的性状进行观察,发现颗粒污泥在启动过程中经历了污泥颗粒裂解到污泥颗粒重组的过程,且厌氧氨氧化颗粒污泥表面含有丰富的官能团,说明厌氧氨氧化颗粒污泥可能具有良好的吸附性能。采用宏基因组测序的方法对启动前后颗粒污泥的生态结构进行分析,发现原接种污泥优势菌群(变形菌门、厚壁菌门、拟杆菌门)丰度大幅减少,厌氧氨氧化菌所属的浮霉状菌门丰度则由1.59%提升到23.24%。     

厌氧氨氧化膨胀床反应器的运行性能

试验研究了以竹炭为载体的厌氧氨氧化膨胀床反应器的运行性能.接种反硝化污泥,用模拟废水可成功启动该反应器:运行至144 d时,容积总氮去除率达到3.02 kg N/m3/d.这是国内文献报道的最高水平.动力学分析表明.这种反应器的最大容积总氮去除率可迭12.77 kg N/m3/d.具有很大的脱氮潜能.反应器的启动过程可分为菌体自溶、活性延滞和活性提高三个阶段.与此相应,污泥性状也从黄褐色絮状污泥变为棕灰色颗粒污泥和红色颗粒污泥.红色颗粒污泥以杆茵和球菌为主.厌氧氨氧化活性可达0.56mg TN/(mgprotein)/h,它们是反应器厌氧氨氧化功能的主要承载者.     

UASB系统启动过程中颗粒污泥形成全过程的机理性分析

ＵＡＳＢ系统启动过程中颗粒污泥形成全过程的机理性分析谢汉方,苏希（辽宁省环境保护科学研究所,沈阳１１００３１）上流式厌氧污泥床（ＵＡＳＢ）作为高负荷厌氧反应器已得到公认,该反应器中培育成的颗粒污泥对提高处理效能极为有效。因此,育成颗粒污泥便成为启动过...     

三种接种物启动Anammox-EGSB反应器的性能

为了优选接种物和加速Anammox反应器启动,分别以厌氧产甲烷污泥 (Anaerobic methanogenic sludge,AMS)、新鲜厌氧氨氧化污泥 (Fresh Anammox sludge,FAS) 和储藏厌氧氨氧化污泥 (Stored Anammox sludge,SAS) 作为接种物,研究了厌氧氨氧化膨胀颗粒污泥床 (Anammox-EGSB) 反应器 (R1、R2和R3) 的启动性能。结果表明：3种接种物均能成功启动Anammox-EGSB反应器,启动性能的优劣次序为：R2 (接种物为     

厌氧氨氧化反应器的启动研究

目的：对UASB-生物膜反应器进行厌氧氨氧化反应的启动研究。方法：以自配含氨氮和亚硝氮的废水为进水,以氧化沟工艺城市污水处理厂回流污泥为接种污泥。结果：反应器内部菌群进行了竞争,在运行至第66d时氨氮、亚硝酸盐氮的去除率分别达到了60.4%、58.7%,同时有硝酸盐氮生成,表明厌氧氨氧化反应已经成为反应器内的主导反应。结论：厌氧氨氧化反应器实现了快速启动。     

ABR结合SBR法处理印染废水的研究

采用实验室规模的厌氧折流板反应器(ABR)与序批式活性污泥曝气反应器(SBR)结合工艺处理印染废水。通过对ABR-SBR处理系统工艺条件的试验,在ABR段HRT为24~36 h,污泥负荷为0.43~2.46 kg COD/(m3.d),进水pH值为6.5~8.0,温度20℃~35℃;SBR段的溶解氧为2 mg/L,曝气时间为3~10 h,沉淀时间为2 h的条件下,经处理的印染工业废水COD、色度和苯胺去除率分别为32%~95%、89%~99%和50%~98%,其COD为30.0~97.1 mg/L,色度为8~40倍,苯胺浓度为0.20~0.95mg/L,达到了国家一级排放标准。     

ABR结合SBR法处理印染废水的研究*

采用实验室规模的厌氧折流板反应器(ABR)与序批式活性污泥曝气反应器(SBR)结合工艺处理印染废水。通过对ABR-SBR处理系统工艺条件的试验,在ABR段HRT为24~36 h,污泥负荷为0.43~2.46 kg COD/(m³.d),进水pH值为6.5~8.0,温度20℃~35℃;SBR段的溶解氧为2 mg/L,曝气时间为3~10 h,沉淀时间为2 h的条件下,经处理的印染工业废水COD、色度和苯胺去除率分别为32%~95%、89%~99%和50%~98%,其COD为30.0~97     

处理印染废水的厌氧折流板反应器中的微生物种群组成及分布规律

设计出一个由12个隔室组成的厌氧折流板反应器(ABR),并将其应用于高浓度、高色度的印染废水生物处理,取得了良好效果。研究着重考察该反应器在处理印染废水过程中不同隔室的微生物种群构成,并分析与印染废水处理效率密切相关的具有脱色功能和苯胺降解功能的两类细菌的分布规律。结果表明,在处理印染废水的ABR反应器中,可培养的优势菌群以芽孢杆菌属(Bacillus)、不动杆菌属(Acinetobacter)、丛毛单胞菌属(Comamonas)、假单胞菌属(Pseudomonas)和水螺菌属(Aquaspirillum)为主,且在ABR的前段、中段及后段隔室中不同种类的优势菌群存在数量差异;好氧及兼性厌氧优势菌群的数量随着废水在ABR隔室中的折流前进而逐渐减少;厌氧微生物的数量变化规律则是先增多,后减少;产甲烷活性在前段隔室中相对较低,后段隔室则相对较高。脱色菌在ABR的前段隔室中分布相对较多,后段隔室中分布相对较少;苯胺降解菌则呈现出在前段隔室中分布相对较少,后段隔室中分布相对较多的规律,这两类功能菌的分布与ABR不同隔室中色度下降、苯胺产生和消减之间密切相关。     

Treatment of low strength complex wastewater using an anaerobic baffled reactor (ABR)

Treatment of a low strength complex wastewater of chemical oxygen demand (COD) around 500mg/L was studied in a 10L capacity laboratory scale anaerobic baffled reactor (ABR). It was operated at hydraulic retention times (HRTs) of 20, 15, 10, 8 and 6h. Corresponding organic loading rates (OLRs) were 0.6, 0.8, 1.2, 1.5 and 2kg COD/m(3)d. At every HRT (or OLR), pseudo steady state (PSS) was achieved. Even at maximum OLR of 2kg COD/m(3)d, COD and biochemical oxygen demand (BOD) removals exceeded 88%. Removal of particulate fraction of organics was found to be greater than soluble fraction. Compartment-wise studies of various parameters revealed that if the OLR was larger, the number of initial compartments played significant role in the removal of organics. The values of volatile fatty acids (VFA) demonstrated that hydrolysis and acidogenesis were the main biochemical activities in the initial few compartments. Based on the tracer studies, dead space in the ABR was found to range from 23% to 34%. The flow pattern in the ABR was classified as intermediate between plug flow and perfectly mixed flows. Observations from scanning electron micrographs (SEM) also suggested that distinct phase separation takes place in an ABR. Study of organic and hydraulic shock loads revealed that ABR was capable of sustaining the type of shock loads generally experienced at a sewage treatment plant (STP).     

内耳形态学和生理指标对缺铁性肾虚耳聋大鼠模型的评价作用

目的探讨耳蜗显微结构和生理指标对缺铁性肾虚耳聋大鼠模型的评价作用。方法选用体重30～32 g、无耳疾、听性脑干反应(auditory brainstem response,ABR)阈值正常的1～2周龄SPF级SD大鼠120只,雌雄分养,分为缺铁组80只、正常对照组40只,饲养时间12周;以出现肾虚证和至少一耳ABR阈值≥15 dB,作为判断肾虚耳聋的标准,获得缺铁性肾虚耳聋大鼠22只,从中选取肾虚耳聋大鼠20只,同时以20只正常大鼠作对照。观察耳蜗血管纹、螺旋器等耳蜗显微结构变化,检测ABR阈值以及血红蛋白和血清铁等指标的变化。结果实验组和正常对照大鼠的血红蛋白和血清铁分别为11.80 g/L,4.5μmol/L和45.9 g/L,22.23μmol/L,ABR阈值分别为(30±5)dB和(10±5)dB;实验组血管纹血管明显减少;螺旋器毛细胞听毛有缺失、倒伏现象。结论缺铁性肾虚耳聋大鼠血红蛋白、血清铁和ABR阈值,以及耳蜗血管纹、螺旋器等耳蜗显微结构变化等指标,均较为稳定,是较好的评价指标。     

软儿梨果酒发酵过程中挥发性风味物质变化分析

软儿梨是西北地区特有的一种“冻果”产品,酸甜可口、果香浓郁,是酿造果酒的上乘原料。为明确果酒发酵过程中果香的保留情况,并探究发酵时间的延长对软儿梨果酒品质的影响,以青海省民和县软儿梨冻果为原料,基于带皮渣发酵工艺,先采用顶空固相微萃取（solid?phase microextraction, SPME）,再结合气相色谱?质谱联用技术（gas chromatography?mass spectrometry, GC?MS）对原汁（0 d）、前发酵（7、14、28 d）、后发酵（100 d）3个不同时期样品中挥发性风味物质进行了动态跟踪分析,并结合相对气味活度值（relative odor activity value,ROAV）和主成分分析（principal component analysis,PCA）法分别探讨了软儿梨果酒原果香味保留情况和后发酵时间的延长对果酒风味的影响。结果显示：整个发酵过程共检出88种挥发性化合物,其中酯类33种、醇类29种、酸类6种、萜烯类7种以及13种其他类化合物,且风味物质的总含量随发酵的进行呈先上升后略有下降的趋势。ROAV结果表明：软儿梨原汁关键风味物质共8种,分别是丁酸乙酯、己酸乙酯、2?甲基丁酸乙酯、正辛醇、大马士酮、芳樟醇、丁香酚和癸醛;其中果香物质己酸乙酯、正辛醇、芳樟醇、丁香酚和大马士酮在果酒发酵中得到了很好的保留,是决定软儿梨果酒风味的关键物质。主成分分析表明：发酵初期主要的香气贡献物质是具有水果香的丁酸乙酯、3?羟基丁酸乙酯、2?甲基丁酸乙酯;发酵100 d时,乙酸乙酯、α?松油醇、柠檬烯和芳樟醇对香气贡献较大,这些香气化合物共同赋予软儿梨果酒幽香清雅、馥香浓郁的独特风味品质。研究获得了软儿梨果酒关键风味物质及其在不同发酵阶段特征风味物质的变化规律,可为研发高品质软儿梨果酒产品、改进软儿梨果酒发酵工艺提供理论支撑和参考。     

Performance and characteristics of an anaerobic baffled reactor

The performance and the characteristics of a laboratory scale anaerobic baffled reactor (ABR) were investigated using synthetic wastewater. The experimental results showed that among different volatile fatty acids (VFAs), acetate was the main intermediate of acidogenic degradation of glucose. The VFA concentration decreased longitudinally down the reactor. The analysis of the biogas composition revealed that methane concentration increased steadily from compartment 1 to 5, while hydrogen content decreased in the first compartments. There was no detectable hydrogen in the last two compartments. The methane-producing activity of anaerobic sludge in different compartments depended on the substrate, which suggests that the proper anaerobic consortium in each separate compartment was developed according to the substrate(s) availability and the specific environmental conditions. The ABR has the potential to provide a higher efficiency at higher loading rates and be applicable for extreme environmental conditions and inhibitory compounds.     

Biochemical indication of microbial mass changes using ATP and DNA measurement in biological treatment of thiocyanate

This study was designed to monitor changes in the levels of adenosine 5'-triphosphate (ATP) and deoxyribonucleic acid (DNA) per unit of microbial mass during the autotrophic biodegradation of thiocyanate (SCN(-)). An artificial medium containing trace minerals and 500 mg SCN(-)/L was used as a substrate for bacterial growth. An SCN(-)-degrading bioreactor with a working volume of 6 L, equipped with temperature, pH, and dissolved oxygen controls, was operated in batch mode. During the exponential phase of SCN(-) biodegradation, the ratios of ATP and DNA to microbial dry weight varied from 0.6 to 1.1 mug ATP/mg of volatile suspended solid (VSS), and from 3.5 to 8.8 mug DNA/mg of VSS, respectively. The ATP and DNA concentrations correlated linearly with microbial mass (r (2) > 0.9) within the exponential phase. The linear regression equations were as follows: (1) microbial mass concentration (mg/L) = 0.663 x ATP concentration (mug/L) + 11.1 and (2) microbial concentration (mg/L) = 0.081 x DNA concentration (mug/L) + 10.9. The applicable ranges were 6.8 to 47.4 mug/L for ATP concentration and 41.5 to 395 mug/L for DNA concentration, respectively.     

Anaerobic Digestion of Dairy Manure in a Hybrid Reactor with Biogas Recirculation

Summary A novel anaerobic hybrid reactor (AHR) configuration incorporating floating support media for biomass immobilization and biogas recirculation for enhanced mixing was used for anaerobic digestion of dairy manure. No pretreatment or solid liquid separation was applied. The reactor was operated at high influent volatile solids (VS) and organic loading rates (OLR) of up to 9.87% and 7.30 g VS/l day, respectively. After 149 days of continuous operation the results revealed that a high amount (38.1 g VSS) of biomass was able to attach itself to the support medium being used. The investigated AHR configuration achieved COD, BOD, TS, and VS removal efficiencies of 48–63, 64–78, 55–65, and 59–68%, respectively, at a hydraulic retention time (HRT) of 15 days. The corresponding average methane production value obtained in this study was 0.191 l/g VS added.     

BOD5 and COD removal and sludge production in SBR working with or without anoxic phase

The aim of this study was to estimate the BOD(5) and COD removal efficiency and biomass yield coefficient in sequencing batch reactors (SBR) treating landfill leachate. Experiments were carried out in four SBRs at HRT of 12, 6, 3 and 2d. Two series were performed. In series 1, the reactors were operated in a 24h cycle mode (anoxic 3h, aeration 18 h, settling 2.75 h, and discharge 0.25 h). In series 2, however, the anoxic phase was eliminated. In both series the BOD(5) removal efficiency was almost identical--over 98%. On shortening HRT from 12 to 2d, COD removal efficiency decreased from 83.1% to 76.7% (series 1). In series 2, efficiency ranged from 79.6% to 75.7%. In the reactors working with the anoxic phase the observed biomass yield coefficient (Y(obs)) was nearly constant (0.55-0.6 mg VSS/mg COD). Upon elimination of the anoxic phase, the Y(obs) was observed to decrease from 0.32 mg VSS/mg COD (HRT 2d) to 0.04 mg VSS/mg COD (HRT 12d).     

Evaluation of biological nutrient removal from wastewater by Twin Circulating Fluidized Bed Bioreactor (TCFBBR) using a predictive fluidization model and AQUIFAS APP

A two-phase and three-phase predictive fluidization model based on the characteristics of a system such as media type and size, flow rates, and reactor cross sectional area was proposed to calculate bed expansion, solid, liquid and gas hold up and specific surface area (SSA) of the biofilm particles. The model was subsequently linked to 1d AQUIFAS APP software (Aquaregen) to model biological nutrient removal in two phase (anoxic) and three phase (aerobic) fluidized bed bioreactors. The credibility of the proposed model for biological nutrient removal was investigated using the experimental data from a Twin Circulating Fluidized Bed Bioreactors (TCFBBR) treating synthetic and municipal wastewater.The SSA of bio-particles and volume of the expanded bed were simulated as a function of operational parameters. Two-sided t-tests demonstrated that simulated SCOD, NH₄-N, NO₃-N, TN, VSS and biomass yields agreed with the experimental values at the 95% confidence level.     

Performances of a full-scale novel multiplate anaerobic reactor treating cheese whey effluent

A 450-m(3) multiplate anaerobic reactor (MPAR) has been started-up in April 1992 for treating wastewater (whey permeate and domestic wastewater) at the Nutrinor (Lactel) cheese factory in Chambord (Québec, Canada). The MPAR consists of four superimposed sections. The liquid flows upwards from one section to the next, while the gas is collected below each plate and evacuated through side-outlets. The wastewater is concurrently distributed at the bottom of the first, second, and third sections, as 50%, 33%, and 17% of the total influent stream, respectively. Granular anaerobic sludge at an initial concentration of 30 kg of volatile suspended solids (VSS) per cubic meter of reactor liquid volume was used to inoculate the reactor. Under normal operation of the factory, the chemical oxygen demand (COD) concentration of the influent ranged from 20 to 37 kg COD m(-3). The reactor organic loading rate (OLR) fluctuated between 9 and 14.7 kg COD m(-3) d(-1) for hydraulic retention times (HRT) maintained between 55 and 68 h. At the highest OLR, the MPAR showed an efficiency of 98% and 92% for soluble and total COD removal, respectively, and a methane production rate averaging around 4 m(3) m(-3) d(-1).Biomass-specific activities ranged between 7 and 51, 1.3 and 8.5, 5.3 and 12.2, 60 and 119, and 119 and 211 mmol g(-1) VSS d(-1) for glucose, propionate, acetate, formate, and hydrogen, respectively. Average equivalent-diameter of the granules was around 0.65 mm. The MPAR reactor generally showed a large capacity for solid retention with a biomass content between 32 and 37 kg VSS m(-3). (c) 1995 John Wiley & Sons, Inc.     

白花草木犀地上部分挥发油的化学成分

白花草木犀(Melilotus alba Medic.ex Desr.)又名白香草木犀、白甜车轴草、辟汗草,原产欧亚温带地区,世界各国均有栽培,在中国西北、华北和东北均有悠久的栽培历史。白花草木犀普遍用作牧草[1],适合在湿润和半干燥气候地区生长,适宜种植于偏碱性土壤上,耐瘠薄、耐盐碱、抗寒和抗旱能力均较强,可作为绿肥及用于盐碱地、瘠薄地的改良[1-2]。白花草木犀药用价值较高,具有清热解毒、利湿、敛阴止汗的功效,用于