膜生物反应器中的生物学特征

由于在膜生物反应器内膜的截留作用 ,使膜生物反应器内的一些生物学特征与传统的活性污泥过程有所不同。本文系统地阐述了膜生物反应器内的微生物群落、活性污泥及微生物产物的生理生化特征。     

焦磷酸测序技术及应用

焦磷酸测序（pyrosequencing）技术是一种新的DNA序列分析技术,其特点是操作简便、大通量、自动化,适合大量样本的快速检测,无须进行电泳、DNA序列无须荧光标记等,是一个理想的遗传分析技术平台.文章对焦磷酸测序技术原理及近年来在单核苷酸多态性研究、微生物鉴定分型和DNA甲基化等方面的应用作一简要综述.     

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。     

微型生物反应器与高通量菌种筛选

生物技术和生命科学将成为21世纪引发新科技革命的重要推动力量,人类所面临的健康、疾病、食品、医药制造、能源、环境等一系列问题成为这一时期最重要的内容。以微生物发酵技术为核心的新一代工业生物技术正在发挥越来越重要的作用,功能菌株（高产菌种）的构建与大规模筛选技术被列为重点研究的新一代工业生物技术之一。     

有机污染土壤生物修复的生物反应器技术研究进展

人类广泛的工农业生产活动常常导致土壤污染。常见的土壤污染有重金属污染和有机污染。近年来 ,世界各国开始重视污染土壤的治理。处理方式主要包括热处理 (焚烧法 )、物理及物理化学处理(洗涤 )和生物处理 (生物修复技术 )。其中生物修复技术被认为最有生命力[1,7] 。目前 ,国外采用的土壤生物修复技术有原位处理、场上处理和生物反应器。生物反应器技术能够有效地发挥生物法的特长 ,是污染土壤生物修复技术中最有效的处理工艺 ,但该技术尚处于实验室研究阶段 ,未广泛应用于现场处理。本文就国外使用生物反应器治理有机污染土壤的研究进展…     

高通量微型生物反应器的研究进展

近年来,哺乳动物细胞培养技术发展迅猛,基于此技术的生物制药行业更是异军突起。在激烈的生物药市场竞争中,缩短研发时间和降低研发成本是制胜的关键。与传统的生物反应器相比,高通量微型生物反应器具有操作简单、运行通量高、实验重复性好等优点,可大大缩短研发周期,降低人力、物力成本,因此成为了生物制药行业最新的研究热点之一。目前,已成功应用于生物药物研发的微型生物反应器有Simcell ^TM、Ambr 15 ^TM、Ambr 250 ^TM等,分别适用于工艺开发中的不同阶段。以上述三种微型生物反应器为例,介绍高通量微型反应器在哺乳动物细胞培养工艺开发中的研究现状及发展前景。     

生物反应器法处理油泥污染土壤的研究

采油过程产生的油泥是整个石油烃污染源的重点。在陆地生态环境中 ,烃类的大量存在往往对植物的生物学质量产生不利影响 ,更重要的是石油中的一些多环芳烃是致癌和致突变物质 ,这些致癌和致突变的有机污染物进入农田生态系统后 ,在动植物体内逐渐富集 ,进而威胁人类的生存和健康[1 ,1 1 ] 。大量的废弃油泥 ,不仅污染农田 ,同时也给石油行业带来巨大的经济损失。污染土壤的治理主要有物理、化学和生物 (生物修复 )方法 ,生物修复方法被认为最有生命力。污染土壤生物修复技术主要有 3种 ,即原位处理、挖掘堆置处理和反应器处理。反应器处理是…     

生物沸石反应器在微污染水源水处理中的应用

随着我国经济社会的发展,水资源短缺和水质问题已成为制约发展的重要因素。因此,必须加强城市污水治理、提高再生水利用率。传统生物滤池在处理污水和再生水的过程中存在诸多问题,如占地面积大、易堵塞等。本文通过使用天然斜发沸石制备的生物沸石反应器进行试验研究,结果显示沸石具有良好的选择性和污染物去除效果,且抗冲击负荷能力强。得到主要结论如下：通过静态吸附试验得出当进水浊度小于5 NTU时,沸石出水浊度可降至0.2 NTU以下;当进水CODMn质量浓度大于3 mg/L时,沸石出水CODMn质量浓度均低于4 mg/L;当进水氨氮质量浓度小于8mg/L时,沸石出水氨氮浓度均低于1 mg/L。说明沸石具有良好的选择性。     

生物反应器法处理PAHs污染土壤的研究

利用自行设计的生物泥浆反应器研究了多环芳烃 (PAHs)污染土壤生物修复技术 .结果表明 ,在相同环境条件下 ,污染物自身的理化性质是影响生物修复的关键因素 ,苯环越多、分子量越大 ,越难以被微生物利用 ,故菲 (PHE)比芘 (PY)具有更高的污染可修复性 .温度、空气流量是重要的调控因子 .本实验中 ,生物泥浆反应器处理PAHs污染土壤选择的最佳运行工艺参数是 :温度 2 0～ 30℃ ,水土比 2∶1,空气流量8L·h-1·L-1,接种量 5 0g·kg-1.该工艺参数为生物泥浆反应器技术实用化及其他相关研究工作的深入开展提供了理论依据     

两级AO膜生物反应器法在白酒生产废水处理中的应用

白酒生产废水由于进水水质波动大、有机物含量高,难以得到有效处理.两级AO膜生物反应器法作为一项新技术,具有处理效果好、能适应水质波动的优点.文章首先介绍了两级AO膜生物反应器法的原理和特点;其次通过实际应用案例分析,发现利用两级AO膜生物反应器法可以有效处理白酒生产废水,使其达到排水水质标准;最后展望了两级AO膜生物反应器法在白酒生产废水处理中的进一步应用.     

Recent advances in membrane technologies for biorefining and bioenergy production

The bioeconomy, and in particular, biorefining and bioenergy production, have received considerable attention in recent years as a shift to renewable bioresources to produce similar energy and chemicals derived from fossil energy sources, represents a more sustainable path. Membrane technologies have been shown to play a key role in process intensification and products recovery and purification in biorefining and bioenergy production processes. Among the various separation technologies used, membrane technologies provide excellent fractionation and separation capabilities, low chemical consumption, and reduced energy requirements. This article presents a state-of-the-art review on membrane technologies related to various processes of biorefining and bioenergy production, including: (i) separation and purification of individual molecules from biomass, (ii) removal of fermentation inhibitors, (iii) enzyme recovery from hydrolysis processes, (iv) membrane bioreactors for bioenergy and chemical production, such as bioethanol, biogas and acetic acid, (v) bioethanol dehydration, (vi) bio-oil and biodiesel production, and (vii) algae harvesting. The advantages and limitations of membrane technologies for these applications are discussed and new membrane-based integrated processes are proposed. Finally, challenges and opportunities of membrane technologies for biorefining and bioenergy production in the coming years are addressed.     

Pyrosequencing analysis of bacterial communities in drinking water biofilters receiving influents of different types

Biological activated carbon (BAC) filters are commonly used in the world for improvement of drinking water quality. The indigenous microbiota in BAC filters can play a crucial role in reduction or biotransformation of contaminants. Molecular analysis can enhance our understanding of ecological functions of the microbial communities in drinking water BAC filters. In this study, three laboratory-scale drinking water BAC filters receiving influents of different types were constructed. Differences of bacterial communities in the three BAC filters were characterized using 454 pyrosequencing analysis. Pyrosequencing analysis illustrated the usefulness in elucidating the bacterial community structure in drinking water biofilter. High bacterial diversity in granular activated carbon (GAC) samples from each BAC biofilter was observed. Proteobacteria was the largest bacterial phylum in each GAC sample, with a marked shift of the proportions of Alpha-, Beta-, and Gammaproteobacteria. The levels of dissolved organic carbon and ammonia nitrogen in the influents could affect the bacterial diversity and community composition in the BAC biofilters. This work might add some new insights into microbial community and its influential factors in drinking water biofilters.     

Characterizing membrane foulants in MBR with addition of polyferric chloride to enhance phosphorus removal

The effect of polymeric ferric chloride (PFC) addition on phosphorus removal and membrane fouling were investigated in an anoxic/oxic submerged membrane bioreactor. The total phosphorus concentration in effluent averaged at 0.26 mg/L with PFC addition of 10-15 mg/L, while the rate of membrane fouling increased 1.6 times over the control MBR (without PFC addition). Three-dimensional excitation-emission matrix fluorescence spectroscopy and Gel Filtration Chromatography analysis indicated that soluble microbial byproduct-like materials and large molecules (M(W)>100 kDa) were one of the main contributors of biofouling. Fourier transform infrared spectrum confirmed that the major components of the cake layer were proteins and polysaccharides materials. Scanning electron microscopy demonstrated that membrane surfaces were covered with compact gel layer formed by organic substances and Energy Dispersive X-ray analysis indicated that ferric metals were the most important inorganic pollutants. Consequently, soluble organic substances and dose of PFC should be controlled to minimize membrane fouling.     

添加不同益生菌对草鱼养殖水体菌群结构的影响

为评价添加不同益生菌对草鱼养殖水体菌群结构的影响,研究采用454焦磷酸测序技术分析其水体菌群结构。结果表明：添加益生菌后的处理组（枯草芽孢杆菌BS、光合细菌PSB和复合菌CB）其微生物多样性高于对照组（Control）。在门的水平,Control和CB样品中变形菌（Proteobacteria）为优势菌,PSB和BS中变形菌（Proteobacteria）和放线菌（Actinobacteria）所占比例差别不大。与Control相比,其他三组中拟杆菌（Bacteroidetes）和放线菌（Actinobacteria）都增加。对变形菌深入分析发现,在PSB,BS和 CB 样品中,-变形杆菌为优势菌,接下来是-变形杆菌纲、-变形杆菌纲和-变形杆菌纲。对拟杆菌分析发现,除对照外,其他样品中黄杆菌纲（Flavobacteria）为优势菌。在对照和处理组中,-变形杆菌、-变形杆菌、-变形杆菌和拟杆菌门在目的水平组成也有差异。以上结果表明,水体中添加益生菌能增加水体菌群多样性,改变菌群结构。     

Influence of membrane fouling reducers (MFRs) on filterability of disperse mixed liquor of jet loop bioreactors

The effects of membrane fouling reducers (MFRs) (the cationic polyelectrolyte (CPE) and FeCI₃) on membrane fouling were studied in a lab-scale jet loop submerged membrane bioreactor (JL-SMBR) system. The optimum dosages of MFRs (CPE dosage = 20 mg g⁻¹MLSS, FeCI₃ dosage = 14 mg g⁻¹MLSS) were continuously fed to JL-SMBR system. The soluble and bound EPS concentrations as well as MLSS concentration in the mixed liquor of JL-SMBR were not changed substantially by the addition of MFRs. However, significant differences were observed in particle size and relative hydrophobicity. Filtration tests were performed by using different membrane types (polycarbonate (PC) and nitrocellulose mixed ester (ME)) and various pore sizes (0.45-0.22-0.1 μm). The steady state fluxes (J_ss) of membranes increased at all membranes after MFRs addition to JL-SMBR. The filtration results showed that MFRs addition was an effective approach in terms of improvement in filtration performance for both membrane types.     

Prediction of membrane fouling in MBR systems using empirically estimated specific cake resistance

The focus of this study was to empirically estimate the specific cake resistance (SCR) by the variation in shear intensity (G) in four laboratory-scale MBRs. The control reactor (MBR₀) was operated with aeration only while other MBRs (MBR₁₅₀, MBR₃₀₀ and MBR₄₅₀) were operated with aeration and mechanical mixing intensities of 150, 300 and 450 rpm, respectively. It was found that the SCR was strongly correlated (R² = 0.99) with the fouling rates in the MBRs. Moreover, the contribution of cake resistance (R_c) to the total hydraulic resistance (R_t) was predominant compared to the irreversible fouling resistance (R_f). On this basis, the cake filtration model was selected as a predictive tool for membrane fouling. This model was modified by replacing the SCR with its empirical shear intensity relationship. The modified model can predict the fouling rate for a given shear intensity (G) within 80 and 250 s⁻¹ in a MBR system.     

A hybrid anaerobic membrane bioreactor coupled with online ultrasonic equipment for digestion of waste activated sludge

Anaerobic membrane bioreactor and online ultrasonic equipment used to enhance membrane filtration were coupled to form a hybrid system (US-AnMBR) designed for long-term digestion of waste activated sludge. The US-AnMBR was operated under volatile solids loading rates of 1.1-3.7 gVS/L·d. After comprehensive studies on digestion performance and membrane fouling control in the US-AnMBR, the final loading rate was determined to be 2.7 gVS/L·d with 51.3% volatile solids destruction. In the US-AnMBR, the improved digestion was due to enhanced sludge disintegration, as indicated by soluble matter comparison in the supernatant and particle size distribution in the digested sludge. Maximum specific methanogenic activity revealed that ultrasound application had no negative effect on anaerobic microorganisms. Furthermore, implementing ultrasound effectively controlled membrane fouling and successfully facilitated membrane bioreactor operation. This lab-scale study demonstrates the potential feasibility and effectiveness of setting up a US-AnMBR system for sludge digestion.