膜生物反应器技术处理洗浴废水的工程应用

根据洗浴废水的水质水量，设计了生物接触氧化和膜生物反应器相结合的处理工艺(水量为120m^3／d)。通过对工艺相关设计参数的选取和调试运行结果表明，该工艺具有处理效果稳定、抗冲击负荷强以及操作简便等优点。     

生化反应工程与工艺研究进展

对生化反应工程现状及发展趋势进行了综述 ,并着重对生物反应器工程的地位、研究内容、研究方法进展、新型生物反应器的开发前景等作了介绍。同时还简要地介绍了生物技术及工艺的研究现状     

生物流化床预处理黄浦江原水中试研究

对采用悬浮填料的生物流化床原水预处理技术进行了探讨。分析了自然挂膜条件下的工艺启动过程。在8个工况条件下，流化床对污染物的去除效果。中试运行表明；在温度适谊，停留时间为60min，填料填充率为50%条件下，氨氮平均去除效率达到77.6%。氨氮的比表面去除负荷与温度线性相关。相关系数为0.911;CODMn平均去除率为6.5%。中试装置在温度10.6℃条件下，重启动需要4d，即对污染物有较好的去除效果；由于填料的完全流化，池体内溶解氧传质效率高，出水接近饱和溶解氧；进出水浊度变化不大。填料和池体本身不会积泥，不需反冲洗。     

转笼式悬浮填料生物反应器启动性能试验

为了研究转茏式悬浮填料生物反应器的启动性能，简化其启动工艺，进行了常温和变温时的反应器的自然挂膜启动实验。实验结果表明，转笼式悬浮填料生物反应器构造的特定微环境有利于自然挂膜，启动比传统生物转盘快10d以上：经过启动参数优化，在水流量为2m^3／h，曝气量为3．6m^3／h、转笼转速为1．5r／min时，启动效果较好。     

组合填料-膜生物反应器处理生活污水生产性试验

在一体式膜生物反应器（MBR）中加入组合填料，对北京某国际公寓的生活污水处理进行了生产性试验。试验表明，在进水水温15～22℃，pH值6．5～7．2，曝气气水体积比9～10：1，COD198．6～563．5mg／L，NH4-N20．5～55．3mg／L，反应器中混合液悬浮固体浓度（MLSS）维持在5200～7800mg／L时，MBR对水中的COD、NH4^＋-N平均去除率分别为90．6％、68．7％，出水中检测不出SS和大肠菌群，浊度小于1NTU，水质满足CJ2511-89《生活杂用水水质标准》。在相同条件下，未加填料反应器MLSS平均值必须维持在12000mg／L以上时才能达到类似处理效果。由于反应器中加入组合填料，降低了MLSS的浓度，减少了膜污染，在膜通量不变情况下，化学清洗周期可延长35～40d。     

Enzymatic modification of canola/palm oil mixtures: Effects on the fluidity of the mixture

The bioreactor system to interesterify edible oils and fats at an ultra-micro aqueous phase of 100 ppm and less was investigated. The adsorption of lecithin, together with lipase onto a carrier, was effective for conducting the interesterifying reaction efficiently for oils and fats in micro aqueous phase. To improve the handling properties of palm oil at rather low temperature, palm oil was blended with canola or soybean oil, and then these blended oils were modified by enzymatic selective interesterification in a solvent-free, ultra-micro aqueous bioreactor system with an immobilized lipase that had 1,3-positional specificity. The effects of enzymatic interesterification were confirmed by triglyceride determination, by solid fat content profiles and by cloud point profiles, which were also compared to products of chemical interesterification. The improvement in the fluidity of blended oils with canola oil by the enzymatic reaction was bigger than with soybean oil, and chemical interesterification had no effects on the fluidity of blended oils.     

两液相生物反应器研究进展

介绍了两液相反应器的进展及存在问题，两液相反应器仍处于试验阶段，其主要问题是生物催化剂在界面的聚集损失活性等。     

固定化微生物细胞降解邻苯二甲酸二丁酯

The biodegradation of di-n-butyl phthalate （DBP） using immobilized microbial cells was carded out in an internal airlift loop reactor with ceramic honeycomb supports. A strain that is capable of degrading DBP was isolated from the activated sludge and identified as Bacillus sp. using 16S rDNA sequential analysis. Bacillus sp. could be rapidly attached onto the ceramic honeycomb supports. The immobilized cells could effectively degrade DBP in batch and continuous experiments. When the influent concentration of DBP was 50mg·L^-1, the effluent DBP reached less than lmg.L i with 6h hydraulic retention time （HRT） in continuous experiment. The immobilized microbial cells could grow and accumulate through the biodegradation of DBP, and the rate of degradation is accordingly increased. The possible pathway of DBP biodegradation using immobilized cells was tentatively proposed.     

用Fenton试剂-矿化垃圾生物反应器联合处理离子交换树脂再生废水

研究了Fenton试剂-矿化垃圾生物反应器联合处理离子交换树脂再生废水.研究结果表明：当原水CODCr为413 mg/L和过氧化氢投加量为24 mL/L（废水）时,经Fenton试剂预处理后,再经矿化垃圾生物反应器后续生化处理（运行周期为4 h,1 h进水,3 h落干,进水流量为600 mL/h）,出水CODCr降至85 mg/L左右,达到国家排放标准.     

一体式膜生物反应器柱式膜组件的临界通量

采用一体式膜生物反应器,考察了4种不同膜丝长度(0.3、0.5、0.7和1.0 m)的柱式膜组件在不同曝气量下的临界通量.研究发现:膜组件的长度存在最优值,膜组件的临界通量同时受到膜丝长度和曝气强度两个方面的影响;当膜组件的膜丝长度为0.7 m时,临界通量最高;同时曝气强度越大,膜组件可以达到的临界通量越高.