附加回流的生物接触氧化工艺净化滇池大清河水质的示范工程研究

针对滇池流域污染最为严重的大清河,采用附加回流生物接触氧化工艺（IBCOP）开展河道水体的旁路处理示范工程研究。IBCOP示范工程的设计规模为1 000 m³/d,HRT为4.75 h,在2007年11月至2008年4月冬旱季期间,根据气候和进水水质条件调节回流比,示范工程运行了3种工况。研究结果表明：示范工程对COD和NH⁺₄-N具有较高的去除效果,平均去除率为46.8%和48.8%,高回流比有利于去除NH⁺₄-N;受到低温、低碳源、高进水DO和生物膜生长不佳等因素影响,示范工程对TN去除效果较低,平均去除率为10.2%,调节回流比不能显著改善碳源不足的情况;水绵的吸收和底泥的沉积是示范工程除磷的主要机理,TP平均去除率为17.9%,低TP浓度进水、生物膜的脱落以及高回流比不利于除磷。     

强地震动作用下地基土-地铁隧道结构的动力接触效应

将地基土-地铁隧道结构体系视为平面应变问题,采用记忆型嵌套面粘塑性动力本构模型和动塑性损伤模型,分别模拟土体和隧道结构混凝土的动力特性,用点-线接触单元模型描述强地震动作用下地基土-地铁隧道之间的相对滑移,利用罚函数法和拉格朗日乘子法求解动力接触效应,建立土-地铁隧道非线性动力相互作用的有限元分析模型,分析了动力接触效应对地基土-地铁隧道之间的法向接触压应力、切向接触剪应力和切向滑移的影响规律。结果表明:罚函数法比拉格朗日乘子法更适用于求解强地震动作用下地基土-地铁隧道之间的动力接触问题;与地基土-地铁隧道变形协调假定的计算结果相比较,动力接触效应使地铁隧道的地震加速度反应有所增大。     

筑坝反滤料动模量和阻尼比试验的颗粒流模拟

以筑坝反滤料的室内中型动三轴试验结果为基础,运用离散单元法中的二维颗粒流方法建立了轴对称数值试样模型,通过控制加荷过程中试样体积不变的方法,模拟了不排水加载条件下反滤料的动模量和阻尼比试验。调整颗粒的细观接触参数,与真实试验结果进行比较分析,在得到符合实际结果的宏观力学响应的同时,分析了配位数、孔隙率和超孔隙水压的变化,并从微观角度对动三轴试验进行了探讨。讨论了固结比和密实度对动模量的影响,认为粗粒反滤料的固结比对最大动模量的影响比较符合H ard in推导公式的结果。结果表明,颗粒流方法可以较好地模拟反滤料的动模量和阻尼比试验,试验过程中微观方面的表现也符合实际室内试验的规律。     

UASB+AF-生物接触氧化工艺处理皂素-酒精综合废水

采用水解酸化-UASB+AF-接触氧化工艺处理黄姜皂素-酒精综合废水,经调试启动和运行研究,结果表明:当进水COD在10 000~12 800 mg/L时,最终出水COD浓度可降低到200 mg/L以下;水解酸化、UASB+AF和接触氧化各阶段的COD去除率分别达到23%、75%和93.5%,系统总的COD去除率可达到98.4%,出水色度在30~50倍之间;同时该工艺具有运行稳定、耐冲击负荷能力强等特点。     

城市轨道交通接触网绝缘子的老化与防护

本文对应用在直流牵引供电系统中接触网绝缘子的老化成因进行了分析,提出接触网绝缘子的防老化手段,并对绝缘子的耐污能力和系统绝缘提出了建议。     

Oxidation of a PAH polluted soil using modified Fenton reaction in unsaturated condition affects biological and physico-chemical properties

A batch experiment was conducted to assess the impact of chemical oxidation using modified Fenton reaction on PAH content and on physico-chemical and biological parameters of an industrial PAH contaminated soil in unsaturated condition. Two levels of oxidant (H₂O₂, 6 and 65 g kg⁻¹) and FeSO₄ were applied. Agronomic parameters, bacterial and fungal density, microbial activity, seed germination and ryegrass growth were assessed. Partial removal of PAHs (14% and 22%) was obtained with the addition of oxidant. The impact of chemical oxidation on PAH removal and soil physico-chemical and biological parameters differed depending on the level of reagent. The treatment with the highest concentration of oxidant decreased soil pH, cation exchange capacity and extractable phosphorus content. Bacterial, fungal, and PAH degrading bacteria densities were also lower in oxidized soil. However a rebound of microbial populations and an increased microbial activity in oxidized soil were measured after 5 weeks of incubation. Plant growth on soil treated by the highest level of oxidant was negatively affected.     

Understanding the granulation process of activated sludge in a biological phosphorus removal sequencing batch reactor

The granulation of activated sludge was investigated using two parallel sequencing batch reactors (SBRs) operated in biological nitrogen and phosphorus removal conditions though the reactor configuration and operating parameters did not favor the granulation. Granules were not observed when the SBR was operated in biological nitrogen removal period for 30 d. However, aerobic granules were formed naturally without the increase of aeration intensity when enhanced biological phosphorus removal (EBPR) was achieved. It can be detected that plenty of positive charged particles were formed with the release of phosphorus during the anaerobic period of EBPR. The size of the particles was about 5-20 μm and their highest positive ζ potential was about 73 mV. These positive charged particles can stimulate the granulation. Based on the experimental results, a hypothesis was proposed to interpret the granulation process of activated sludge in the EBPR process in SBR. Dense and compact subgranules were formed stimulated by the positive charged particles. The subgranules grew gradually by collision, adhesion and attached growth of bacteria. Finally, the extrusion and shear of hydrodynamic shear force would help the maturation of granules. Aerobic granular SBR showed excellent biological phosphorus removal ability. The average phosphorus removal efficiency was over 95% and the phosphorus in the effluent was below 0.50 mg L⁻¹ during the operation.     

猪场废水厌氧发酵液循环脱氮工艺

研究了水解酸化与生物接触氧化组合循环工艺处理猪养殖场废水厌氧发酵液的脱氮特性,重点考察了组合工艺的最佳运行工况和参数,同时讨论了组合工艺低温运行的性能。结果表明,水力停留时间24 h和污水循环比1∶3为最佳运行工况,此时出水氨氮浓度为2.16～8.20 mg/L。溶解氧(DO)浓度2～3 mg/L和有机负荷3 g/L以下为最佳运行参数,出水氨氮浓度稳定在10 mg/L以下。在春季低温条件下(8～12℃),组合工艺也能较好运行,水解酸化池内小分子有机酸产生总量为114.50～244.22 mg/L。组合工艺连续运行3个月以上,污染物去除效果稳定。     

BCO+BAF工艺深度处理洗涤剂废水

采用生物接触氧化(BCO)+曝气生物滤池(BAF)组合工艺深度处理洗涤剂废水,研究了溶解氧浓度(DO)、水力停留时间(HRT)对其处理性能的影响。实验结果表明,随着DO浓度的提高,组合工艺对COD和LAS的去除率都随之增加;水力停留时间的增加有利于对COD与LAS的去除,最佳停留时间选为21.2h为宜;在BCO段DO为3.0 mg/L,HRT为20.0 h,BAF段DO为4.0 mg/L,HRT为1.2 h的运行条件下,COD与LAS的去除率分别为90.5%和94.3%,出水COD和LAS均能达到排放标准。     

阿科蔓介质生物接触氧化法预处理微污染原水

随着库区经济的发展,大量点源或面源污染物未经有效处理便直接排入水体致使许多可作为生活饮用水的水源变成了"微污染"水源,鉴于常规的预处理工艺不能很好地适应现有"微污染"水源水质的变化,采用挂膜成功的阿科蔓介质生物接触氧化法对微污染水源水进行预处理实验研究,并与挂膜成功的组合介质生物接触氧化法进行对比,结果表明,阿科蔓介质挂膜速度较快,效果较好,且对水源水质的变化具有较好的适应性,是微污染水原水质改善较为理想的人工介质;对于相同的微污染水源,阿科蔓介质的处理效果明显优于组合介质且处理效果良好,其对"微污染"水源水中TN、氨氮、COD和总磷的平均去除率分别为67.4%、87.2%、54.1%和40.1%,其中较适宜的阿科蔓介质生物接触氧化预处理进水溶解氧浓度为4.0~6.0 mg/L。阿科蔓介质生物接触氧化不失为一种开展饮用水源地生态防护与饮用水质改善的技术。