连续流膜生物反应器中好氧颗粒污泥的形成及机制探讨

为了探讨好氧颗粒污泥在连续流膜生物反应器(MBR)中的形成过程和机制,采用连续流试验的方法,研究了好氧颗粒污泥形成过程中膜反应器内污染物的去除效果和好氧颗粒污泥特性的变化,并对连续流MBR中好氧颗粒污泥的形成机制进行了探讨.结果显示,连续流MBR中好氧颗粒污泥的形成增强了MBR的运行稳定性和抗冲击能力.废水中微生物抑制...     

利用PCR-DGGE溯源典型农村塘坝饮用水中的污染

以华南地区典型农村塘坝饮用水为研究对象,采用基于大肠杆菌的两种特异性基因(β-D-葡萄糖苷酶编码基因uidA和膜外周磷通道蛋白编码基因phoE)的群体差异分析(PCR-DGGE),对饮用水中的污染情况进行了溯源研究.结果表明,采用富集培养的混合菌体DNA作为模板扩增大肠杆菌特异性基因更加实用.uidA和phoE的引物均...     

Chemical cleaning of fouled PVC membrane during ultrafiltration of algal-rich water

Cleaning of hollow-fibre polyvinyl chloride (PVC) membrane with di erent chemical reagents after ultrafiltration of algal-rich water was investigated. Among the tested cleaning reagents (NaOH, HCl, EDTA, and NaClO), 100 mg/L NaClO exhibited the best performance (88.4% 1.1%) in removing the irreversible fouling resistance. This might be attributed to the fact that NaClO could eliminate almost all the major foulants such as carbohydrate-like and protein-like materials on the membrane surface, as confirmed by Fourier transform infrared spectroscopy analysis. However, negligible irreversible resistance (1.5% 1.0%) was obtained when the membrane was cleaning by 500 mg/L NaOH for 1.0 hr, although the NaOH solution could also desorb a portion of the major foulants from the fouled PVC membrane. Scanning electronic microscopy and atomic force microscopy analyses demonstrated that 500 mg/L NaOH could change the structure of the residual foulants on the membrane, making them more tightly attached to the membrane surface. This phenomenon might be responsible for the negligible membrane permeability restoration after NaOH cleaning. On the other hand, the microscopic analyses reflected that NaClO could e ectively remove the foulants accumulated on the membrane surface.     

Catalytic bubble-free hydrogenation reduction of azo dye by porous membranes loaded with palladium nanoparticles

Catalytic bubble-free hydrogenation reduction of azo dye by porous membranes loaded with palladium （Pd） nanoparticles was studied for the first time. The effects of Pd loading, dye concentration and reuse repetitions of membranes were investigated. In reduction, the dye concentration decreased whereas the pH rose gradually. An optimal Pd loading was found. The catalytic membranes were able to be reused more than 3 times.     

Fouling distribution in forward osmosis membrane process

Fouling behavior along the length of membrane module was systematically investigated by performing simple modeling and lab-scale experiments of forward osmosis （FO） membrane process. The flux distribution model developed in this study showed a good agreement with experimental results, validating the robustness of the model. This model demonstrated, as expected, that the permeate flux decreased along the membrane channel due to decreasing osmotic pressure differential across the FO membrane. A series of fouling experiments were conducted under the draw and feed solutions at various recoveries simulated by the model. The simulated fouling experiments revealed that higher organic （alginate） fouling and thus more flux decline were observed at the last section of a membrane channel, as foulants in feed solution became more concentrated. Furthermore, the water flux in FO process declined more severely as the recovery increased due to more foulants transported to membrane surface with elevated solute concentrations at higher recovery, which created favorable solution environments for organic adsorption. The fouling reversibility also decreased at the last section of the membrane channel, suggesting that fouling distribution on FO membrane along the module should be carefully examined to improve overall cleaning efficiency. Lastly, it was found that such fouling distribution observed with co-current flow operation became less pronounced in counter- current flow operation of FO membrane process.     

陶粒CANON反应器的接种启动与运行

通过CANON接种污泥,以人工配制无机高氨氮废水为对象,研究以陶粒为填料的CANON反应器启动与运行情况,结果表明:①陶粒可以作为CANON反应器合适填料,温度通过水浴控制在30℃±1℃,HRT为9 h、pH控制在7.00~8.08之间,经过60 d成功启动了CANON反应器,TN的去除负荷达到0.79 kg·(m3·d)-1;②在温度30℃时,陶粒CANON反应器中临界DO范围在1.12~1.69 mg·L-1之间,CANON反应器中短程硝化和厌氧氨氧化性能可维持稳定,高于此范围时,会出现CANON反应器中短程硝化不稳定现象;③在温度25℃,控制DO在1.01~1.54 mg·L-1之间时,尽管NO-3-N变化值与TN变化值的比值(δNO-3-N/δTN)略微偏离理论值0.127,为0.150~0.204,但CANON反应器脱氮性能趋于稳定,TN去除率最高为75.56%,TN的去除负荷最高达到0.97 kg·(m3·d)-1,这意味着CANON工艺的适宜温度范围至少可以降低至25℃.     

曝气膜生物反应器运行过程中污泥活性特征变化及其对膜污染的影响

研究了曝气膜生物反应器运行过程中活性污泥主要活性特征变化及其对膜污染的影响.通过排出剩余污泥的办法维持活性污泥浓度在4000 mg·L-1左右,并连续运行75 d.运行期间,每日检测活性污泥的各项性质指标便于反映污泥特性的变化.结果表明,随着反应器运行时间的延长,污泥脱氢酶活性逐渐增加,其对反应器的运行有着两方面的作用,一方面会强化微生物对污染物的去除,但另一方面则导致了胞外聚合物的增加,并加速膜污染.而污泥表观产率则随着运行时间的延长先增加后有所减少,其粒径逐渐减小,且胞外聚合物呈现增加的趋势,总的出水水质情况逐渐提高,与此同时,反应器内原生动物及后生动物在运行前期较少,而在后期大量出现.膜污染分析结果表明运行后期膜污染速度明显加快,其原因在于:污泥粒径的减小以及胞外聚合物的增加导致细小颗粒及胞外聚合物堵塞或在膜表面沉积数量增加.     

低强度超声波强化SMBR处理中的超声波参数优化研究

研究了利用低强度超声波强化低温一体式膜生物反应器（SMBR）污水生物处理中最优超声波参数的选择。结果表明,功率密度为0.27 W/L、辐照时间为20 min时,超声波对低温SMBR中COD去除的强化效果最佳。SMBR对NH3-N去除效果达到最佳时,超声波功率密度和辐照时间分别为0.27 W/L和15 min。综合考虑,选择更有利于低温时NH3-N去除的超声波参数：功率密度0.27 W/L、辐照时间15 min。经此超声波处理后COD、NH3-N的强化效果在24 h均能保持,故可设置超声波处理的时间间隔为24 h。     

膜污染层微生物与聚丙烯微滤膜间的界面作用及其吸附特征

采用热力学方法及界面吸附理论,对2株膜污染层微生物(Aeromonas veronii M4、Aeromonas caviae N25)与聚丙烯(PP)微滤膜间的界面作用及吸附特征进行研究.结果表明,Aeromonas veronii M4与PP膜表面均表现出明显的疏水性特征,而Aeromonas caviae N25则呈现亲水性特征,并且A.veronii M4的运动性能也要高于A.caviae N25;另外,2株细菌及PP膜的表面均带有负电荷,表现出明显的电子供体特征,而Lewis酸碱分量U_(mlb)~(AB)则在2株细菌与PP膜的界面作用能中占据着主导地位;依据XDLVO理论,A.caviae N25及A.veronii M4与PP膜之间的总界面作用能均为负值,表明二者在膜上的吸附是一个主动吸附过程,而A.veronii M4-PP膜之间的界面作用能负值最大,说明A.veronii M4具有较高的吸附能力;静态吸附结果则表明,A.veronii M4在PP膜上的吸附量要明显高于A.caviae N25,而2株菌在膜上的吸附行为可由准二级动力学模型进行描述.     

大渡河干海子滑坡稳定性研究

干海子滑坡位于大渡河流域,规模巨大.为研究该滑坡的稳定性,在对滑坡基本特征及变形破坏特征等深入研究的基础上,采用极限平衡法(Geo-slope软件)和有限差分法(FLAC-3D软件)对该滑坡的稳定性和应力应变特征进行了计算、模拟.稳定性计算模拟主要从深层、浅层及局部稳定三方面入手分析,计算模拟结果与滑坡的宏现地质现象均...