MBR运行初期对基因工程菌的截留特性研究

在膜-生物反应器(MBR)中实施基因工程菌生物强化时,运行初期基因工程菌流失是生态风险评价的重要内容.在一体式微滤膜-生物反应器中,考察了运行初期不同运行条件对基因工程菌流失密度和截留效率的影响,并对截留特性进行了探讨.结果表明,膜-生物反应器运行初期,不同运行条件对基因工程菌的截留效率影响不同:污泥浓度增加,截留效率提高;提高膜通量和曝气量,截留效率降低.基因工程菌接种密度为1.0×1010CFU/mL时,不同运行条件下的流失密度为1.0×102 CFU/mL～2.5×102 CFU/mL,最大截留效率大于8 lg.膜-生物反应器运行初期,膜组件截留、污泥吸附以及对悬浮细胞迁移阻碍是影响截留效率的主要因素,一定条件下其截留效率贡献率分别为82.3%、14.9%和2.8%.膜-生物反应器稳定运行过程中形成凝胶层,可以提高截留效率.一定条件下,膜组件、污泥和凝胶层对基因工程菌的截留贡献率分别为75.3%、10.7%和14.0%.     

基因工程菌在活性污泥中的衰减及其影响因素

在间歇实验和连续运行的反应器中,考察了基因工程菌细胞密度在活性污泥中的衰减,进行了动力学模型拟合,求得模型参数,并分析了影响衰减的因素.结果表明,在间歇实验和连续运行反应器中,细胞密度在活性污泥中均呈现初期快速衰减而后趋于稳定的趋势.其衰减动力学可以用Logistic模型和Gompertz模型拟合,两个模型的拟合都有很好的相关性和显著性,拟合优度没有差异.在不同的条件下,间歇实验拟合得到的参数取值范围是：Logistic模型衰减系数r′=0.5～0.6 h^-1,稳定细胞密度K′=10⁴～10⁵ cfu·ml^-1;Gompertz模型初始衰减系数b=0.6～1.2 h^-1,比衰减系数a=0.02～0.09 h^-1.初始投加密度对衰减速率影响不大,但是显著影响稳定细胞密度.污泥浓度和温度对衰减速率和稳定密度均有显著影响. 污泥浓度越大,衰减越快,稳定密度越大;而温度越低,衰减越快,稳定密度也会越低.营养条件和微型动物捕食也是影响衰减的重要因素.基因工程菌在连续运行的膜生物反应器和活性污泥反应器中的细胞密度衰减,也可以用Logistic模型拟合,其参数在间歇实验的取值范围内.     

膜-生物硝化反应器处理含氨废水效能的研究

研究了膜 生物硝化反应器对含氨废水的处理效能以及分离膜的截留和渗透效能。膜_生物反应器启动迅速 ,在水力停留时间为 1d的情况下 ,反应器最高进水浓度达 80mmol(NH₄⁺-N)·L^-1 ,最高容积负荷达 1 12kg(NH₄⁺ -N)·m^-3·d^-1 ,氨氮去除率保持在 95%以上。试验证明 ,分离膜对微生物有良好的截留作用 ,50天内反应器的污泥浓度从 5g·L^-1 增长到 10g·L^-1 ,分离膜表面附着的生物层则对废水氨氮和亚硝氮有进一步的转化作用。在液位差低于 80cm时 ,提高液位差可增大膜渗透通量 ;液位差超过 80cm后 ,增大液位差的膜渗透通量效应很小 ;其中 ,当液位差为 2 0cm左右时 ,膜通量达 2 . 5 1L·m^-2 ·h^-1 ,阻力最小 [(2 . 6 3× 10^-5)m^-1]。该膜_生物硝化反应器可依靠液位差压力驱动出水 ,无需外加动力。     

序批式反应器不同活性污泥特性的比较研究

研究了以厌-好氧交替运行方式序批式反应器(SBR)中接种普通活性污泥(CAS)、膜生物反应器(MBR)污泥、好氧颗粒污泥(AGS)的特性,研究结果表明,三种类型的污泥表现出不同的特性.     

綪纶纤维接枝改性后抗菌作用的实验观察

目的　观察经接枝改性后 FFA- 3和 FFS- 1纤维织物的抗菌作用。方法　采用容器振荡法 ,溶液为生理盐水 ,纤维含量为 2 .5 % ,受试菌接种量为 10 5～ 10 6 CFU/ml,作用 12 h。结果　 2种纤维中的大肠埃希菌存活菌数均为 0 ;葡萄球菌存活菌数分别是 1.0 2× 10 4和 4.16× 10 3CFU/m l。而对照纤维中 2种受试菌存活菌数分别为 1.6× 10 5 CFU/ml和 2 .99× 10 4CFU/m l。结论　 FFA- 3和 FFS- 1纤维织物有一定的抗菌作用     

膜生物反应器的研究进展

膜生物反应器是近年来发展的废水处理新技术,具有活性污泥浓度高、污泥龄长、占地面积小、投资省的特点。利用膜生物反应器进行污水处理不仅可以大大节约水资源,还可以大大节约能源,节省设备和运行费用,已成为二十一世纪研究热点。膜生物反应器是通过高效膜分离技术与活性污泥相结合,增大污泥中的特效菌来加快生化反应速率,提高废水处理效果。目前处理对象已从生活污水扩展到高浓度的有机废水和难降解的工业废水。本文综述了膜生物反应器在废水中的应用研究情况,并分析比较了各种膜材质的特点、适用范围以及膜的污染因素和清洗方法,展望了膜生物反应器的应用前景及进一步研究方向。     

厌氧E-MBR反应器在焦化废水处理中的微生物特性研究

【目的】将厌氧的膜生物反应器(MBR)与微生物燃料电池(MFC)耦合的厌氧电辅助膜生物反应器(E-MBR)应用于实际工业焦化废水处理。【方法】通过正交实验优化了反应器进水的培养条件为PO_4~(3–)14.3 mg/L、Fe~(2+)0.2 mg/L、Fe~(3+)0.1 mg/L、Co~(2+)0.1 mg/L和Mn~(2+)0.2 mg/L。在此条件下考察了该反应器对系统中有机污染物的去除效率及厌氧污泥的污泥特性、产电性能、胞外聚合物(EPS)、微生物群落结构及膜污染的影响。【结果】结果表明,与未优化的培养条件相比,工业焦化废水COD的去除率提高了23%;污泥浓度(MLSS)、比重、沉降速度增加,污泥体积指数(SVI)降低,表明污泥颗粒化及沉降性能提高;污泥中溶解性EPS (SMP)、松散态EPS (LB-EPS)及紧密结合态EPS (TB-EPS)这3种组分中的蛋白质与多糖的比例(P/C)分别降低0.12、0.25和0.16,表明污泥更易于被降解;厌氧污泥的产电性能增强;高通量分子测序结果表明,反应器中污泥的群落结构发生了明显的变化,优势菌群突出;经扫描电镜(SEM)对比结果表明,反应器阴极膜的污染情况也得到了一定的减缓。【结论】优化进水培养条件可以达到使反应器污水处理效率提高、清理周期缩短和运行更稳定等效果,对于工业废水处理技术的节能环保方面提供一定的理论依据。     

固定化细胞膜反应器生产6－APA的研究

将青霉素酰化酶基因工程菌大肠杆菌A56(pPA22)通过交联截留固定化在由中空纤维膜或平板膜构成的膜反应器内,提高了单位体积反应器的酶活,实现了高浓度青霉素的裂解。采用反冲模式操作的中空纤维膜反应器裂解7．8％医用青霉素钠盐50批,产品6－APA的平均重量收率达到90．1％,纯度达98．6％,50批反应操作后,膜反应器内剩余酶活力仍在80％以上。     

初始接种量对Bt33菌株孢子含量的影响

在温度 30± 0 5℃、转速 180r/min的条件下 ,用Bt发酵培养液对Bt33菌株进行振荡培养 ,考察不同接种量和液培时间对孢子含量的影响。结果表明 ,将孢子含量为 2 5× 10 9CFU ml的母液按 1%～ 15 % (V V)的比例接种后培养 33～ 5 0h ,9%和 12 %接种量处理能产生 8 5× 10 9CFU ml以上的孢子浓度。通过拟合逻辑斯蒂生长模型 ,发现该菌在上述液培条件下的最大孢子含量为 1 0 3× 10 1 0 CFU ml。     

豆腐废水UASB反应器中的原核生物多样性及主要功能菌群

通过构建16S rRNA基因文库,对豆腐废水UASB反应器中颗粒污泥的原核生物多样性进行了分析,并用MPN法对颗粒污泥中的互养产乙酸细菌和产甲烷菌进行了活菌数量测定。结果表明,33%的16S rRNA基因序列属于产甲烷菌,氢和乙酸盐营养型的产甲烷菌在颗粒污泥中数量最多,分别为1.1×10.9个/mL和4.5×10.8个/mL。低GC革兰氏阳性菌和δ-变形菌纲分支的细菌也是颗粒污泥中的主要菌群,它们的16S rRNA序列分别占22%和9%,其中互养产乙酸细菌在颗粒污泥中的数量可达4.5×10.7个/ml。绿色非硫细菌是另一类丰度很高的细菌,其16S rRNA序列占文库的12%。对各类微生物在颗粒污泥中可能的作用进行了讨论。通过研究不仅了解了特定环境中的微生物组成,还为从中分离特异类群的微生物提供了指导。     

Organics and nitrogen removal and sludge stability in aerobic granular sludge membrane bioreactor

Novel aerobic granular sludge membrane bioreactor (GMBR) was established by combining aerobic granular sludge technology with membrane bioreactor (MBR). GMBR showed good organics removal and simultaneous nitrification and denitrification (SND) performances for synthesized wastewater. When influent total organic carbon (TOC) was 56.8-132.6 mg/L, the TOC removal of GMBR was 84.7-91.9%. When influent ammonia nitrogen was 28.1-38.4 mg/L, the ammonia nitrogen removal was 85.4-99.7%, and the total nitrogen removal was 41.7-78.4%. Moreover, batch experiments of sludge with different particle size demonstrated that: (1) flocculent sludge under aerobic condition almost have no denitrification capacity, (2) SND capacity was caused by the granular sludge, and (3) the denitrification rate and total nitrogen removal efficiency were enhanced with the increased particle size. In addition, study on the sludge morphology stability in GMBR showed that, although some granular sludge larger than 0.9 mm disaggregated at the beginning of operation, the granular sludge was able to maintain the stability of its granular morphology, and at the end of operation, the amount of granular sludge (larger than 0.18 mm) stabilized in GMBR was more than 56-62% of the total sludge concentration. The partial disaggregation of large granules is closely associated with the change of operating mode from sequencing batch reactor (SBR) system to MBR system.     

Process efficiency and microbial monitoring in MBR (membrane bioreactor) and CASP (conventional activated sludge process) treatment of tannery wastewater

In this study a pilot-scale membrane bioreactor (MBR) and a conventional activated sludge plant (CASP), treating the same tannery wastewaters and in the same operating conditions, have been compared in order to evaluate the overall treatment efficiency, the presence and distribution of Gram negative bacteria and the kinetics of nitrifying bacteria. Process efficiency was evaluated in terms of organic and nitrogen compounds: the MBR showed a higher COD removal (+4%) and a more stable and complete nitrification. The Gram negative bacteria were detected by fluorescent in situ hybridization (FISH) with phylogenetic probes monitoring of alpha-, beta- and gamma-Proteobacteria, of the main ammonia-oxidizing bacteria (AOB) and nitrite-oxidizing bacteria of the Nitrobacter and Nitrospira genera. The results showed that the main differences between the two sludges were: the higher abundance of alpha- and gamma-Proteobacteria in the MBR bioreactor and the presence of AOB aggregates only on the surfaces of MBR flocs. Finally, the titrimetric (pH-stat, DO-stat) tests showed similar values of the kinetic parameters of the nitrifiers both in MBR and CASP sludge.     

Reduction in excess sludge production in a dairy wastewater treatment plant via nozzle-cavitation treatment: Case study of an on-farm wastewater treatment plant

Nozzle-cavitation treatment was used to reduce excess sludge production in a dairy wastewater treatment plant. During the 450-d pilot-scale membrane bioreactor (MBR) operation, when 300 l of the sludge mixed liquor (1/10 of the MBR volume) was disintegrated per day by the nozzle-cavitation treatment with the addition of sodium hydrate (final concentration: 0.01% W/W) and returned to the MBR, the amount of excess sludge produced was reduced by 80% compared with that when sludge was not disintegrated.     

短程硝化启动运行中功能菌群变化研究

【目的】短程硝化-厌氧氨氧化是可实现的最短生物脱氮工艺,短程硝化是实现该工艺的重要环节和必要条件。【方法】采用序批式反应器(SBR)来实现短程硝化过程的启动和稳定运行,并对该过程中的相关功能菌群变化进行检测分析。【结果】通过控制低DO浓度(<1 mg/L)和逐步提高氨氮进水负荷,可抑制氨氧化细菌(NOB)菌群增殖并促进亚硝酸氧化菌(AOB)菌群规模显著扩大,实现短程硝化过程的启动和稳定运行。在氨氮进水负荷为0.055 kg/(m3.d)时,平均氨氮去除容积负荷和污泥负荷可达到0.043kg/(m3.d)和0.16 kg/(kg.d),平均亚硝酸盐积累率可达到83.4%。在短程硝化启动和稳定运行过程中,NOB菌群密度从2.0×105CFU/mL降至1.5×104CFU/mL,相对丰度从5.51%降至2.14%;AOB菌群密度从4.5×104CFU/mL增加至1.5×107CFU/mL,相对丰度从0.18%增加至7.25%。【结论】AOB菌群规模的扩大是实现短程硝化和氨氮去除能力提高的主要原因,同时较高的进水氨氮浓度和负荷也会造成亚硝化活性的抑制。     

Sewage treatment by a low energy membrane bioreactor

A new membrane bioreactor (MBR) was developed for treatment of municipal wastewater. The MBR was mainly made up of an activated sludge reactor and a transverse flow membrane module, with an innovative configuration being in application between them. As a result, the transverse flow membrane module and low recirculation flow rate created advantages, such as lower energy consumption and more resistance to membrane fouling. The total energy consumption in the whole system was tested as 1.97+/-0.74 kWh/m(3) (permeate) while using periodical backwash with treated water and backflush with mixed liquor daily, being in the same level as a submerged membrane bioreactor, reported to be 2.4 kWh/m(3) (permeate). Energy consumption analysis in the system shows that the membrane module was more energy consuming than the other four parts listed as pump, aeration, pipe system and return sludge velocity lose, which consumed 37.66-52.20% of the total energy. The effluent from this system could be considered as qualified for greywater reuse in China, showing its potential application in the future.     

Biological hydrogen production using a membrane bioreactor

A cross-flow membrane was coupled to a chemostat to create an anaerobic membrane bioreactor (MBR) for biological hydrogen production. The reactor was fed glucose (10,000 mg/L) and inoculated with a soil inoculum heat-treated to kill non-spore-forming methanogens. Hydrogen gas was consistently produced at a concentration of 57-60% in the headspace under all conditions. When operated in chemostat mode (no flow through the membrane) at a hydraulic retention time (HRT) of 3.3 h, 90% of the glucose was removed, producing 2200 mg/L of cells and 500 mL/h of biogas. When operated in MBR mode, the solids retention time (SRT) was increased to SRT = 12 h producing a solids concentration in the reactor of 5800 mg/L. This SRT increased the overall glucose utilization (98%), the biogas production rate (640 mL/h), and the conversion efficiency of glucose-to-hydrogen from 22% (no MBR) to 25% (based on a maximum of 4 mol-H(2)/mol-glucose). When the SRT was increased from 5 h to 48 h, glucose utilization (99%) and biomass concentrations (8,800 +/- 600 mg/L) both increased. However, the biogas production decreased (310 +/- 40 mL/h) and the glucose-to-hydrogen conversion efficiency decreased from 37 +/- 4% to 18 +/- 3%. Sustained permeate flows through the membrane were in the range of 57 to 60 L/m(2) h for three different membrane pore sizes (0.3, 0.5, and 0.8 microm). Most (93.7% to 99.3%) of the membrane resistance was due to internal fouling and the reversible cake resistance, and not the membrane itself. Regular backpulsing was essential for maintaining permeate flux through the membrane. Analysis of DNA sequences using ribosomal intergenic spacer analysis indicated bacteria were most closely related to members of Clostridiaceae and Flexibacteraceae, including Clostridium acidisoli CAC237756 (97%), Linmingia china AF481148 (97%), and Cytophaga sp. MDA2507 AF238333 (99%). No PCR amplification of 16s rRNA genes was obtained when archaea-specific primers were used.     

不同入流条件下植被过滤带对坡面径流氮、磷的拦截效果

植被过滤带能有效拦截坡面径流泥沙,在防治水土流失和农业面源污染等方面具有重大潜力.为探讨不同入流条件下植被过滤带对坡面径流氮、磷的拦截效果及其水动力学机理,本研究通过模拟上方来水冲刷试验,定量分析了上方来水流量、氮磷含量浓度等因素影响下植被过滤带对径流氮、磷的拦截规律及其与径流水动力学参数之间的关系.结果表明: 植被过滤带能有效拦截上方来水中氮、磷等污染物,入流流量分别为200、400、600 L·h^-1时,模拟植被过滤带对总氮的拦截率分别为74.9%、62.0%、58.3%,对总磷拦截率分别为85.0%、75.6%、72.0%,在上方来水流量较低时拦截效果最优;上方来水入流氮、磷浓度变化对植被过滤带拦截效率的影响不显著.不同入流条件处理下,植被过滤带对氮、磷的拦截率随弗洛德数增大而增大,呈显著线性正相关关系;与阻力系数、水流剪切力、水流功率呈线性负相关关系;其中,氮、磷拦截率与水流剪切力的相关关系最优,可以用含水流剪切力的公式表征植被过滤带对氮、磷的拦截效率.     

Change in the fouling propensity of sludge in membrane bioreactors (MBR) in relation to the accumulation of biopolymer clusters

A membrane bioreactor (MBR) and an activated sludge process (ASP) were operated side by side to evaluate the change of sludge supernatant characteristics and the evolution of the sludge fouling propensity. The MBR sludge had a higher organic concentration and more biopolymer clusters (BPC) in the supernatant compared with ASP. BPC increased in both concentration and size in the MBR. The results show that the change in the liquid-phase property had a profound effect on the sludge fouling propensity. MBR operation transformed typical activated sludge to MBR sludge with a higher fouling propensity. Distinct from the ASP, membrane filtration retained soluble microbial products (SMP) within the MBR, and the vast membrane surface provided a unique environment for the transformation of SMP to large size BPC, leading to further sludge deposition on the membrane surface. Thus, membrane filtration is the crucial cause of the inevitable fouling problem in submerged MBRs.     

淡紫紫孢菌PLF-1对感染尖刀镰孢菌百合种球的促生作用及其相关防御酶活性变化

为了探究淡紫紫孢菌(Purpureocillium lilacinum)PLF-1对百合种球的促生作用及对百合尖刀镰孢菌的防治效果,采用平板对峙法评估淡紫紫孢菌对尖孢镰刀菌的拮抗效果,以及淡紫紫孢菌对百合抗尖孢镰刀菌的抗性作用。同时监测百合种球中超氧化物歧化酶（SOD）、过氧化物酶（POD）和过氧化氢酶（CAT）的活性变化情况。研究结果表明：浓度为4.34×10⁴ CFU/mL和4.34×10⁵ CFU/mL的淡紫紫孢菌孢子悬浮液对百合种球表现为促进作用,浓度为4.34×10⁴ CFU/mL时最高茎长达11 cm。平板拮抗实验中该淡紫紫孢菌菌株能有效抑制尖孢镰刀菌生长,抑制率高达72%。接种淡紫紫孢菌和病原菌的百合种球茎长会增长37.6%,根长会增长33%。该菌株能提高感染尖刀镰孢菌百合种球中的超氧化物歧化酶（SOD）、过氧化物酶（POD）和过氧化氢酶（CAT）活性,有效抑制尖刀镰孢菌的毒害作用,促进植株健康生长。