颗粒移动床除尘装置高效粉尘回收器

本文介绍了颗粒移动床除尘装置高效粉尘回收器──雾膜高效旋风分离器的性能、水气比例的确定以及对沸腾锅炉粉尘除尘试验的结果，证明该高效旋风分离器的分高效率高达９９％。     

颗粒移动床除尘系统喷动再生器的研究

文中概要介绍了作者提出了喷动清灰颗粒移动床除尘系统，提出了喷动清灰机理、清灰器设计、结构参数、清灰效率、动力消耗的实验结果；证明了喷动清灰颗粒移动床除尘系统的优越性。     

厌氧污泥床过滤器处理涤纶废水的生产性试验

采用厌氧泥床过滤器 (UASBAF)处理高浓度涤纶废水 ,试验结果表明 :UASBAF反应器具有较高的处理涤纶废水的效能 ,稳定运行容积负荷可达 10～ 12kg/m3 ·d ,水力停留时间 2 2～ 2 4h ,CODCr去除率 80 %左右 ,并具有启动快 ,耐冲击性负荷强的特点。     

湿式颗粒过滤床在中小窑炉消烟除尘中的应用

颗粒过滤床的滤料层粒子排列间隙，是在水膜与气膜高速流动状态互 换，促进粉尘表面附着力，降低黑灰和炭粒接触角，提高疏水性，实现水汽自激，微细粒径凝取和，达到消烟除尘的目的。     

浮床水稻对富营养化水体中氮、磷的的去除效果及规律研究

采用水域浮床无土种植方法，以人工模拟池为试验场所，在池内的富营养水水体表面种植水稻，通过水稻的吸收和吸附作用，去除水体中的Ｎ、Ｐ元素，以实现变废为宝，净化水质，并使水体产生良性循环。     

生物反硝化计量学关系研究

提出了在生物反硝化中可利用有机物与硝酸盐氮消耗量的比值（△COD／△N）建立反硝化计量方程式，以及计算出实际污泥产率{γHdbs=0.614R－1.755[g（VSS）／g（N）]}与最佳碳氮比投加值。分别以葡萄糖与甲醇为电子供体，硝酸盐为电子受体。在上流式反硝化颗粒污泥床内进行实验验证。结果表明，计算值与实测值非常一致。证明该计算方法准确、可行。     

合成洗涤剂废水处理的一种新工艺研究

在合成洗涤剂废水絮凝床预处理技术（ＣＦＢ）的实验研究基础上，成功地应用ＣＦＢ法配以简单的ＳＢＲ生化法处理了该类废水。为合成洗涤剂废水治理开辟了一条新的途径。     

The integration of methanogenesis with denitrification and anaerobic ammonium oxidation in an expaned granular sludge bed reactor

The integration of methanogenesis with denitrification and anaerobic ammonium oxidation (ANAMMOX) was studied in an expanded granular sludge bed (EGSB) reactor in this work. Experimental results from the continuous treatment of wastewater with nitrite and ammonium, which lasted for 107 days, demonstrated that wastewater with high nitrite and ammonium could be anaerobically treated in an expanded granular sludge bed reactor. More than 91% to 97% of COD were removed at up to about 3.9 g COD/(L x d) of COD volumetric loading rate. More than 97% to 100% of nitrite was denitrified at up to about 0.8 g NO2(-) -N/(L x d), which is 16 times higher than that in a conventional activated sludge system with nitrification/denitrification (0.05 gN/(L x d)). No dissimilatory reduction of nitrite to ammonium occurred in the process. However, maximum of about 40% ammonium was found to be lost. Batch tests of 15 days with sludge from the reactor showed that 100% of nitrite was denitrified completely, and about 3% of ammonium was removed when only ammonium (34.3 mg/L) and nitrite (34.3 mg/ L) were added into the sludge suspension medium. Furthermore, about 15% of ammonium amounts were lost with organic COD addition. It suggested that the methanogenesis in the system could enhance ANAMMOX because of intermediate hydrogen produced during methanogenesis.     

悬浮生物填料床处理微污染原水硝化试验研究

对采用新型悬浮填料床处理微污染原水硝化过程进行了探讨分析了自然挂膜条件下的工艺启动过程，研究了不同工况条件下，悬浮填料床硝化效果。通过春、夏、秋和冬季的中试运行效果表明：在温度适宜、停留时间60min、填料填充率50％条件下，氨氮平均去除效率达到77．60％，定义了氨氮填料表面负荷指数判断氨氮去除效果，水温对硝化的影响较大，在低于20℃时，氨氮填料表面负荷随温度呈指数增长，高于该温度时则增长缓慢，但能维持较高水平；浊度对本工艺硝化影响较小；实验表明原水中氨氮浓度较低，硝化反应符合一级反应，其反应速率常数为0.75h^-1。     

电絮凝-生物滤床处理印染废水的试验研究

用电絮凝-生物滤床工艺对印染废水进行了试验研究。结果发现：当电解段的电流密度为3.636mA/cm^2，流量为25mL/min，滤床段的停留时间为100min时，CODcr,NH3-N,TP和色度的去除率分别80.9%,82.4%,89.5%和90%。