硅对过量锰胁迫下水稻根系抗氧化系统和膜脂质过氧化作用的调控机理

揭示Mn胁迫下Si对水稻根系抗氧化系统的影响机制,可为减轻水稻Mn毒害提供重要的理论依据和技术支持.因此,本研究通过水培试验,采用两个对Mn耐性不同的水稻品种,研究Si(1.5 mmol·L-1)对Mn(2 mmol·L-1)胁迫下水稻根系抗氧化系统的影响.结果表明,在Mn胁迫下,敏感品种新香优640(XXY)根系的超...     

Control of membrane fouling during hyperhaline municipal wastewater treatment using a pilot-scale anoxic/aerobic-membrane bioreactor system

Membrane fouling limits the effects of long-term stable operation of membrane bioreactor (MBR). Control of membrane fouling can extend the membrane life and reduce water treatment cost effectively. A pilot scale anoxic/aerobic-membrane bioreactor (A/O-MBR, 40 L/hr) was used to treat the hyperhaline municipal sewage from a processing zone of Tianjin, China. Impact factors including mixed liquid sludge suspension (MLSS), sludge viscosity (μup), microorganisms, extracellular polymeric substances (EPS), aeration intensity and suction/suspended time on membrane fouling and pollution control were studied. The relationships among various factors associated with membrane fouling were analyzed. Results showed that there was a positive correlation among MLSS, sludge viscosity and trans-membrane pressure (TMP). Considering water treatment efficiency and stable operation of the membrane module, MLSS of 5 g/L was suggested for the process. There was a same trend among EPS, sludge viscosity and TMP. Numbers and species of microorganisms affected membrane fouling. Either too high or too low aeration intensity was not conducive to membrane fouling control. Aeration intensity of 1.0 m³/hr (gas/water ratio of 25:1) is suggested for the process. A long suction time caused a rapid increase in membrane resistance. However, long suspended time cannot prevent the increase of membrane resistance effectively even though a suspended time was necessary for scale off particles from the membrane surface. The suction/suspended time of 12 min/3 min was selected for the process. The interaction of various environmental factors and operation conditions must be considered synthetically.     

医院污水处理中可吸附有机卤化物（AOX）及其毒性研究

对序批式膜生物反应器（MBR）处理前后医院污水中的AOX进行了比较,分析了c_Rt值对不同水质中AOX生成量的影响及相应的生物毒性.结果表明,序批式MBR对医院污水中AOX的去除率达到63.6％,其中膜截留占14.5％;要获得相同的c_Rt值,原污水所需的投氯量显著高于MBR出水,相应生成的AOX浓度也较高;通过曲线拟合发现,随着c_Rt的增长,医院原污水中AOX浓度呈指数增长,而MBR出水呈线性关系.以粪大肠杆菌为指示微生物,要达到医院污水微生物排放标准（GB 18466-2005）,医院原污水所需c_Rt为5.5 (mg·h)/L,而MBR出水只需c_Rt为0.007 5 (mg·h)/L,其相应的生物毒性分别为40.39 μg/L和8.96 μg/L (以K₂Cr₂O₇计),AOX浓度分别为607.1 μg/L和102.5 μg/L.     

2-甲基乙酰乙酸乙酯对藻细胞膜和亚显微结构的影响

为揭示化感物质抑制藻类的机理, 研究了芦苇化感物质2-甲基乙酰乙酸乙酯(eathyl-2-methyl acetoacetate, EMA)对蛋白核小球藻、铜绿微囊藻和普通小球藻细胞膜磷脂脂肪酸种类、含量以及藻细胞亚显微结构的影响,采用Bligh and dye法提取藻类细胞膜磷脂脂肪酸,GC-MS测定脂肪酸种类和含量,透射电镜法观测细胞亚显微结构. 结果表明, EMA使蛋白核小球藻细胞膜不饱和脂肪酸亚麻酸、亚油酸含量都增加了14%, 而饱和脂肪酸肉豆蔻酸、棕榈酸含量则下降了12%和11%. 加入EMA后, 铜绿微囊藻细胞膜中不饱和脂肪酸C18∶1和C18∶2含量分别增加了12%和10%, 饱和脂肪酸C18∶0和C16∶0含量则下降. EMA对普通小球藻细胞膜磷脂脂肪酸含量没有显著影响. EMA使蛋白核小球藻和铜绿微囊藻细胞壁脱落, 细胞膜破裂, 细胞内含物渗出, 细胞内片层结构解体, 细胞核和线粒体结构损坏. EMA对普通小球藻细胞亚显微结构没有显著破坏.     

环境水体中肠道病毒的膜吸附-洗脱浓缩方法研究

在膜吸附-洗脱和洗脱液浓缩相结合的基础上,建立了一种简便实用的水中肠道病毒浓缩方法.通过实时定量RT-PCR检测,比较了不同材料和不同孔径的微孔滤膜对病毒的吸附效果;对膜洗脱方式进行了改进;研究了在洗脱液浓缩过程中,PEG浓度对于病毒回收率的影响.最后确定了最佳的浓缩方法.选择效果好而且来源广泛的0.22 μm孔径的混合纤维素酯微孔滤膜,采用磁力搅拌来洗脱滤膜上吸附的病毒;洗脱液浓缩步骤中,PEG最佳质量浓度为130　g/L.系统比较了不同病毒接种量下,方法中各步骤的病毒回收率.对接种已知量的肠道病毒的生活污水、二级处理出水和地表水等样品的试验结果表明,该方法效果稳定,适合不同水样中肠道病毒的浓缩分离.     

MBR处理医院污水后续氯消毒及其消毒副产物研究

针对医院污水中致病微生物的特殊排放要求,研究了膜生物反应器（MBR）应用于医院污水处理中的预消毒及其后续氯消毒特性.结果表明,在工程应用中MBR具有显著的预消毒作用,对医院污水中的细菌总数和粪大肠杆菌的去除率分别达到2.0～3.1 lg和2.8～4.0 lg;对于MBR出水中残留的微生物,采用次氯酸钠进行后续消毒,当接触时间为1 h,在有效氯浓度为0.8 　mg/L时,可检测不出粪大肠杆菌,且放置6 h未见再生长,相应的THMs和HAAs分别为16.94 μg/L和32.10 μg/L;固定接触时间,随着Cl₂/DOC值的增加,MBR出水中THMs和HAAs均近似呈线性增长趋势（r²分别为0.941?5和 0.965?2）,且HAAs的增长速率高于THMs.     

自生动态膜-生物反应器结构优化的研究

针对自生动态膜-生物反应器内部结构进行了动力学运行的理论分析,通过能量平衡机理对自生动态膜-生物反应器体系进行了讨论,基于体系总能耗最小的原理推导出液相循环流动方程.建立的混合液流速与清水流速之间的关系模型可以很好地反映混合液流速与清水流速之间的关系.通过建立的清水流速测定方法得出反应器结构与清水膜面错流流速之间的关系：调整降流区横截面积(A_d)与底部通道截面积(A_b)的比值为0.7以及升流区横截面积(A_r)与顶部通道截面积(A_u)的比值为0.9,调整降流区横截面积与升流区横截面积的比值在1.2～1.5范围内以及增加反应器的有效高度H_D都可以在不改变曝气强度的条件下增加膜面错流速度,此结果与推导出的循环流动方程可以很好地吻合.     

Comparison of membrane fouling during short-term filtration of aerobic granular sludge and activated sludge

Aerobic granular sludge was cultivated adopting internal-circulate sequencing batch airlift reactor.The contradistinctive experiment about short-term membrane fouling between aerobic granular sludge system and activated sludge system were investigated.The membrane foulants was also characterized by Fourier transform infrared(FTIR)spectroscopy technique.The results showed that the aerobic granular sludge had excellent denitrification ability;the removal efficiency of TN could reach 90%.The aerobic granular sludge could alleviate membrane fouling effectively.The steady membrane flux of aerobic granular sludge was twice as much as that of activated sludge system.In addition,it was found that the aerobic granular sludge could result in severe membrane pore-blocking, however,the activated sludge could cause severe cake fouling.The major components of the foulants were identified as comprising of proteins and polysaccharide materials.     

Phytoremediation of urban wastewater by model wetlands with ornamental hydrophytes

Phytoremediation offers a cost-effective,non-intrusive,and safe alternative to conventional cleanup techniques.In this study,we used ornamental hydrophytes plants as constructed wetlands to treat urban or rural domestic wastewater.Most ornamental hydrophytes adapted to the wastewater well,and were fairly efficient in scavenging BOD_5(biological oxygen demand 5 d),COD(chemical oxygen demand),TN(total nitrogen),TP(total phosphorus)and heavy metals(Cr,Pb,Cd)in the wastewater.However,the efficiency varied a lot for various species to different contaminants,Iris pseudacorus L.and Acorus gramineus Soland were good choices for treatment of composite-polluted urban wastewater.Some variation in the change of membrane peroxidation and endogenous protective system in responses to wastewater was found among six hydrophytes,which have a correlation with the efficiency of wastewater treatment.It may demonstrate that the developed antioxidative systems of I.pseudacorus and A.gramineus contributed much to their superiority. On the other hand,interaction of different components in the wastewater might have certain effects on phytoremediation.     

MBR-RO组合工艺深度处理焦化废水试验研究

采用膜生物反应器-反渗透(MBR-RO)组合工艺对二级生化处理后的焦化废水进行深度处理。考察了MBR单元及RO单元对污染物的去除效果,详细探讨了原水电导率、跨膜压差对RO单元产水率和脱盐率的影响。试验结果表明,该组合工艺运行稳定且处理效果好,处理后的出水水质能满足《工业循环冷却水处理设计规范》(GB 50050—2007)的要求。