小直径锥形管成形工艺研究

通过对小直径锥形管的工艺分析 ,介绍了一种成形的工艺方法和措施 ;并就成形、加工模具作了详细说明     

日光辐射对大气真菌粒子的影响

大气中真菌粒子的衰亡和净化，除与真菌自身的因素有关外，与日光辐射也有密切关系。此文现场观测了日光辐射对大气真菌粒子的影响。结果表明，一天内大气真菌粒子浓度与日光辐射强度呈反比：大气真菌粒数直径中值与日光辐射强度呈正比：随着日光辐射强度的增大，＜３．０μｍ的大气真菌粒子，其浓度减小的速度比＞３．０μｍ的快。     

一种新型直流旋风分离器的分离机理探讨

分析了一种新型直流旋风分离器的分离机理及结构特点 ,推导出了这种旋风分离器内颗粒的运动规律和被分离的临界粒径。     

Characteristics of sewer biofilms in aerobic rural small diameter gravity sewers

Small diameter gravity sewers(SDGS) are extensively used to collect rural sewage as they are low in cost and quick to construct.However,the characteristics of biofilms in rural SDGS are still not clear.In this study,biofilms characteristics of aerobic rural SDGS were investigated using simulations in a lab under different flow conditions and slopes.Results indic ated that the average thickness of aerobic rural SDGS biofilms was in the range of 350-650 μm,decreasing at locations with variable flow and high slopes.Protein was the most abundant substance in extracellular polymeric substance of SDGS biofilms.The most abundant bacteria,Proteobacteria,Actinobacteria,and Bacteroidetes,and functional bacteria showed different distributions when analyzed through Illumina HiSeq sequencing of 16 S rRNA.The relative abundances of denitrifying bacteria,nitrite-oxidizing bacteria,and sulfate-reducing bacteria(SRB) were lower during variable flow than during stable flow.High slopes(15‰) decreased SRB presence,which could be used to mitigate H_2 S accumulation in aerobic SDGS.Overall,this study describes the characteristics of aerobic rural SDGS biofilms and provides valuable suggestions for the optimal design of SDGS based on these characteristics.     

水平搅拌下低高径比SBR中好氧活性污泥的颗粒化

在设有水平机械搅拌、高径比（H/D）为1.2的圆柱形鼓风曝气SBR中,考察了活性污泥的颗粒化情况,对成熟颗粒污泥表面所受水力剪切速率进行了定量研究,分析了水平搅拌在颗粒化过程中的作用.结果表明：有水平搅拌存在下污泥逐渐颗粒化,形成了均值粒径为1.12mm的好氧颗粒污泥,污泥沉降速度为21.41m/h;计算结果表明污泥表面所受的平均剪切速率为27.25s^-1,剪切应力为3.38×10^-2N/m²;污泥表面所受平均剪切速率与机械搅拌速率和表观气速均呈正相关关系;实验条件下机械搅拌对剪切速率的贡献要远大于表观气速的贡献,前者指数约为后者的37.48倍.研究认为水平搅拌在反应器中形成的具有足够剪切强度的旋涡二次流是促使低高径比反应器好氧污泥颗粒化的关键水力条件.     

Morphology, growth and carbohydrate storage of the plant Typha angustifolia at different water depths

Morphological characteristics, growth and carbohydrate storage dynamics of Typha angustifolia in relation to water depth were investigated. The study was based on observations carried out in two stands, namely Akigase and Teganuma, for two growth seasons. The latter stand was about two times deeper than the former. Teganuma stands exhibited significantly higher number of thick shoots compared to those of Akigase. Conversely, the difference in shoot heights between the two stands was insignificant. The same was true for rhizome lengths. Rhizome diameters were significantly bigger for Teganuma compared to Akigase. Furthermore, both the above and belowground biomass were significantly higher for Teganuma compared to those of Akigase. Teganuma stands allocated 55% of the total biomass to the aboveground parts, while Akigase stands allocated 60%. Similarly, Teganuma exhibited significantly higher stocks of total non-structural carbohydrates (TNC) compared to Akigase. The higher number of thick shoots and the relatively bigger rhizome diameters in Teganuma are seemingly important tolerance strategies in maintaining effective aeration into the rhizosphere, by reducing internal resistance. In addition, the higher TNC stocks and biomass help not only to enhance survival under anoxia for longer durations, they also provide firm substrate anchorage in the deeper Teganuma stands.     

化学气相沉积法对13X分子筛孔径修饰及吸附性能研究

化学气相沉积法可对１３Ｘ分子筛进行孔径修饰，并用于含重金属离子废水的净化处理。研究结果表明，随１３Ｘ分子筛外表面ＳｉＯ２沉积量的增加，孔径收缩。     

关于环形风道比摩阻两种计算方法

就通风空调工程中具有特殊应用的环形风道的摩擦阻力计算问题进行了分析，根据流体力学原理，提出了采用流量当量直径法和直接利用圆形风道计算图风道的比摩阻2种方法，第2种计算方法与流量当量直径法比较，查表时更直接。     

应用多导流筒气升式环流生物反应器处理化肥工业含氨废水

在天津××化工厂建立了一套反应器有效体积为80m3的低高径比、多导流筒气升式环流生物反应器处理化肥工业含氨废水的装置。针对影响生物硝化效果的影响因素气液比、水力停留时间进行了考察,得到了操作的优化条件气液比为50∶1,水力停留时间为5h。在此条件下,该装置对废水中的COD_(Cr)和NH4+-N的去除率分别在75%和98%以上,出水中COD_(Cr)<50mg/L,NH4+-N<10mg/L。     

常温下IC反应器启动过程中的颗粒污泥性能研究

在常温下用自配葡萄糖废水启动IC反应器,研究了厌氧颗粒污泥的形成过程和特性。IC反应器进水浓度为3 000 mg COD/L,水温为14.5～26℃,25 d内形成了颗粒污泥。结果表明,随着运行时间和容积负荷的增加,颗粒污泥粒径逐渐增大。反应器启动完成后,反应器中2 mm的颗粒污泥增加到6.6%,0.3 mm的颗粒从57.7%减少到39.4%;VSS浓度从24.7 g/L上升到48.2 g/L;VSS/SS从34.4%增加到72.8%。颗粒污泥的沉降速度与颗粒粒径成正比,0.3～3 mm的颗粒污泥的沉降速度介于34.05～109.75 m/h之间,具有良好的沉降性能。初始接种污泥几乎没有产甲烷活性,与第30 d的初期颗粒污泥相比,成熟的颗粒污泥的产甲烷活性提高了46.7%。