农副食品加工业高浓度废水的厌氧膜生物反应器技术

农副食品加工业COD年排放量在41种行业废水中排名第2,污染减排刻不容缓.农副食品加工业废水COD浓度高达8 000~30 000 mg·L-1,目前主要采用厌氧-好氧组合工艺处理,存在工艺流程长、管理难和成本高等问题.厌氧膜生物反应器(anaerobic membrane bioreactor,AnMBR)由于高效的膜与厌氧微生物协同作用,具有COD去除率高(92%~99%),COD负荷率高[2.3~19.8 kg·(m3·d)-1]等工艺特征,同时排泥少(SRT>40 d),基建成本低(HRT为8~12 h).根据高浓度COD的不同构成,COD甲烷化的限速步骤可分为水解酸化限速型、产甲烷限速型.AnMBR的膜污染特征及其控制比好氧MBR更为复杂和困难,现有膜污染控制措施包括错流过滤、曝气冲洗和膜松弛等.针对我国农副食品加工业高浓度废水达标排放的技术需求,AnMBR主要研究方向为提高COD去除率、控制膜污染和提高能源回收率,从而实现短流程厌氧的出水一步达标.     

纳米Ag粒子原位杂化PVDF超滤膜的抗污染性能

以AgNO3为前驱体,聚偏氟乙烯(PVDF)为聚合物基体,聚乙烯吡咯烷酮(PVP)为分散剂和成孔剂,N,N-二甲基甲酰胺(DMF)为还原剂和溶剂,利用相转化法制备了纳米Ag粒子原位杂化PVDF超滤膜.采用扫描电镜、透射电镜、原子力显微镜及接触角测定仪对杂化膜的结构和性能进行了表征.结果表明:原位形成的纳米Ag粒子均匀地分散在聚合物基体中,纳米Ag粒子的添加改善了PVDF膜的亲水性能.以腐殖酸和牛血清蛋白作为污染物的代表,考察了Ag/PVDF膜的抗有机污染性能.以大肠杆菌、耐甲氧西林金黄色葡萄球菌及活性污泥作为微生物的代表,考察了杂化膜的抗生物污染性能.结果证实了与纯PVDF膜相比,Ag/PVDF膜通量衰减较慢,可有效抑制微生物的生长,表面受活性污泥污染程度小,具有显著的抗有机污染和抗生物污染性能.     

不同原水中膜污染物质的表征与确定

本文采用有机物的组分分析、相对分子质量分布及三维荧光等分析手段,研究了青草沙水库和滆湖原水的膜过滤通量的表现,探讨了膜污染的机理.试验结果表明,中亲组分有机物造成的微滤膜和超滤膜的通量下降最为严重,而疏水性有机物对通量的影响甚微.滆湖水对微滤膜的通量下降较青草沙水库水严重,而青草沙水库水对超滤膜的通量下降较滆湖水严重.膜污染机理的分析表明,微滤膜污染主要由膜孔堵塞造成,而超滤膜的通量主要受大分子有机物形成的滤饼层的影响.三维荧光分析表明,蛋白质类的有机物是造成膜污染的主要物质.     

三峡库区消落带3种植物淹水后汞的动态变化及其对水体的影响

被淹没的植物是水库甲基汞异常升高的来源之一.为探寻淹水条件下三峡水库消落带植物中汞的动态变化特征及其对水体的影响,通过室内模拟试验,研究淹水条件下稗草、狗牙根、玉米秸秆中汞含量变化及其向水体释汞情况.结果表明,3种植物总汞含量范围为9.21~12.07 ng·g-1,甲基汞占总汞的质量分数约为1%~2%.淹水后,植物总汞含量逐渐降低,其降幅为35.81%~55.96%;而上覆水溶解态汞(DHg)浓度迅速上升,增幅为103.23%~232.15%,说明植物腐烂分解会向水体释放汞.淹水环境为植物体组织内甲基化提供了充裕条件,导致植物残体甲基汞含量升高,为初始含量的3.04~6.63倍,而上覆水溶解态甲基汞(DMe Hg)浓度也显著升高,为初始浓度的14.84~16.05倍.淹水期间,上覆水中DMe Hg与溶解氧(DO)浓度表现为极显著负相关,与可溶性有机碳(DOC)浓度存在显著正相关.而在整个淹水过程中,上覆水DHg浓度变化量为植物总汞释放量的41.74%~47.01%,且各植物残体总汞含量与上覆水DHg浓度存在极显著负相关.     

Gas separation using porous cement membrane

Gas separation is a key issue in various industrial fields. Hydrogen has the potential for application in clean fuel technologies. Therefore, the separation and purification of hydrogen is an important research subject. CO2 capture and storage have important roles in ＂green chemistry＂. As an effective clean technology, gas separation using inorganic membranes has attracted much attention in the last several decades. Membrane processes have many applications in the field of gas separation. Cement is one type of inorganic material, with the advantages of a lower cost and a longer lifespan. An experimental setup has been created and improved to measure twenty different cement membranes. The purpose of this work was to investigate the influence of gas molecule properties on the material transport and to explore the influence of operating conditions and membrane composition on separation efficiency. The influences of the above parameters are determined, the best conditions and membrane type are found, it is shown that cementitious material has the ability to separate gas mixtures, and the gas transport mechanism is studied.     

Effect of ozone on the performance of a hybrid ceramic membrane-biological activated carbon process

Two hybrid processes including ozonation-ceramic membrane-biological activated carbon （BAC） （Process A） and ceramic membrane-BAC （Process B） were compared to treat polluted raw water. The performance of hybrid processes was evaluated with the removal efficiencies of turbidity, ammonia and organic matter. The results indicated that more than 99% of particle count was removed by both hybrid processes and ozonation had no significant effect on its removal. BAC filtration greatly improved the removal of ammonia. Increasing the dissolved oxygen to 30.0 mg/L could lead to a removal of ammonia with concentrations as high as 7.80 mg/L and 8.69 mg/L for Processes A and B, respectively. The average removal efficiencies of total organic carbon and ultraviolet absorbance at 254 nm （UV254, a parameter indicating organic matter with aromatic structure） were 49% and 52% for Process A, 51% and 48% for Process B, respectively. Some organic matter was oxidized by ozone and this resulted in reduced membrane fouling and increased membrane flux by 25%-30%. However, pre-ozonation altered the components of the raw water and affected the microorganisms in the BAC, which may impact the removals of organic matter and nitrite negatively.     

Anoxic gas recirculation system for fouling control in anoxic membrane reactor

Anoxic gas recirculation system was applied to control the membrane fouling in pilot-scale 4-stage anoxic membrane bioreactor(MBR). In the anaerobic-anoxic-anoxic-aerobic flow scheme,hydrophilic polytetrafluoroethylene(PTFE) membrane(0.2 μm, 7.2 m2/module) was submerged in the second anoxic zone. During 8 months operation, the average flux of the membrane was 21.3L/(m2·hr). Chemical cleaning of the membrane was conducted only once with sodium hydroxide and sodium hypochlorite. Dissolved oxygen(DO) concentration in the second anoxic zone was maintained with an average of 0.19 ± 0.05 mg/L. Gas chromatography analysis showed that the headspace gas in the second anoxic reactor was mainly consisted of N2(93.0% ± 2.5%), O2(3.8% ± 0.6%), and CO2(3.0% ± 0.5%), where the saturation DO concentration in liquid phase was 1.57 mg/L. Atmospheric O2 content(20.5% ± 0.8%) was significantly reduced in the anoxic gas. The average pH in the reactor was 7.2 ± 0.4. As a result, the recirculation of the anoxic gas was successfully applied to control the membrane fouling in the anoxic MBR.     

ABR-MBR一体化工艺节能降耗措施优化研究

能耗高和膜污染是限制膜生物反应器(MBR)广泛应用的重要因素.为降低工艺运行能耗和延缓膜污染,以厌氧折流板反应器(ABR)-MBR工艺处理生活污水为例,对工艺结构和脱氮除磷运行条件进行优化.结果表明,通过优化ABR-MBR工艺结构,可降低43%的运行能耗,同时可保持较高的COD、NH+4-N、TN和TP去除效果,平均去除率分别为91%、85%、76%和86%.另外,添加颗粒填料可有效延缓膜污染,不过也改变了膜污染的形成过程,膜内部污染物含量显著增多,碳水化合物含量增加,而蛋白质含量减少,碳水化合物/蛋白质比明显增大.最终,增强了MBR反应器的实际应用性能.     

Optimal nonpoint source pollution control strategies for a reservoir watershed in Taiwan

The purpose of this study is to develop a model for optimal nonpoint source pollution control for the Fei-Tsui Reservoir watershed in Northern Taiwan. Several structural best management practices (BMPs) are selected to treat stormwater runoff. The complete model consists of two interacting components: an optimization model based on discrete differential dynamic programming (DDDP) and a zero-dimensional reservoir water quality model. A predefined procedure is used to locate suitable sites for construction of various selected BMPs in the watershed. In the optimization model, the objective function is to find the best combination of BMP type and placement, which minimizes the total construction and operation, maintenance, and repair (OMR) costs of the BMPs. The constraints are the water quality standards for total phosphorus (TP) and total suspended solids (TSS) concentrations in the reservoir. A zero-dimensional reservoir water quality model of the Vollenweider type is embedded in the optimization framework to simulate pollutant concentrations in Fei-Tsui Reservoir. The resulting optimal cost and benefit of water quality improvement are depicted by the model-derived trade-off curves. The modeling framework developed in the present study could be used as an efficient tool for planning a watershed-wide implementation of BMPs for mitigating stormwater pollution impact on the receiving water bodies.     

石化企业伤亡事故率的系统动力学仿真

针对石化企业伤亡事故率的复杂性和与企业运行的系统相关性,为了科学地预测伤亡事故率,提出了利用系统动力学对石化企业伤亡事故率进行仿真试验的方法.在对石化企业伤亡事故率进行了系统动力学分析之后,建立了石化企业伤亡事故率系统动力学仿真模型,对某石化企业进行了仿真试验,并分析了仿真试验的结果.试验应用表明,利用系统动力学对石化企业伤亡事故率进行仿真是科学有效的.