改良型氧化沟工艺调试与运行

介绍了娄底市第一污水处理厂一期工程设计概况和采用的改良型氧化沟脱氮除磷工艺,分析了该污水处理厂调试、培菌过程中出现的问题,并针对性地采取了一系列改进措施.在进水远低于设计值的不利条件下,通过合理培菌,不到一个月系统启动成功.监测结果表明:该工艺运行可靠,出水水质稳定、达标.     

大学园区污水生态处理技术工艺及系统设计

详述了大学园区污水生态处理技术的工艺和系统设计问题。通过浮动生物床预处理和潜流湿地或地下毛管渗滤系统的深度处理,可将校园污水转换成为再生水利用,该处理系统具有良好的经济效益和生态效益。     

Modification of Cavitation Air Floatation Equipment for Oxidation Ditch Excess Activated Sludge Thickening

We point out the weak points of oxidation ditch excess activated sludge thickening by cavitation air floatation process. out in this paper and the reasons for such weak points are analyzed, and some advanced measures are put forward and. a mModified cavitation air flotation (MCAF) equipment MCAF 10 for oxidation ditch sludge thickening has been developed. The flocculant FO4440SH with 1.0 kg/tDS was added with 1.0 kg/tDS and the 0.2kg/tDS of the surfactant 1227 were adopted with addition of 0.2kg/tDS. When the CAF 5 was employed to thicken oxidation ditch excess sludge, the optimal solid loading was 230kgMLSS/m3·d, and the hydraulic loading was 90 m2/m3·d, and the SS in the effluent was 200～250mg/L;. When the MCAF 10 was used to thicken oxidation ditch excess activated sludge, the optimal solid loading was 270kgMLSS/m3·d, hydraulic loading was 110 m2/m3·d, and the SS of the effluent was 100～150mg/L. The experimental results indicate that the modified cavitation air flotation (MCAF) equipment is more suitable for sludge thickening.     

CASS工艺在屠宰废水处理中的应用

分析了CASS工艺处理屠宰废水的工程实例 ,指出了其主要构筑物有集水调节池、沉淀池、气浮池、水解酸化池、CASS池和污泥池.主要的工艺为CASS工艺 ,设计工艺具有简单、自动化程度高、占地面积小、运行费用低、处理效率高等优点.     

脉冲电气浮过程中非均匀流场模拟及分析

针对浮选过程中传统电气浮存在大范围剧烈环流,造成泡絮混合物生长和浮上的干扰较大,导致能量利用率低的问题,提出了采用方形脉冲通电的脉冲电气浮的方式,产生非均匀流场,以减轻环流对泡絮混合物的影响,提高能量利用效率.采用Ansys13.0中的Fluent模块对脉冲电气浮气液两相流场进行了模拟.研究结果表明,与常规电气浮相比,脉冲电气浮非均匀湍流场的能量分布更为合理,微气泡上浮过程中产生的环流程度较小,有利于泡絮混合物的形成和浮选过程.在相同电流密度的前提下,脉冲电气浮的耗电量仅为传统电气浮1/4～1/3,且能达到与传统电气浮近似相同的浮选效果,能量利用效率较高.     

Aggregate and organic matter dynamics in reclaimed soils as indicated by stable carbon isotopes

Recovery of belowground ecosystem processes, such as soil aggregation and organic matter (OM) accumulation, in reconstructed soils is crucial to successful reclamation of disturbed lands. Objectives of this study were to track soil aggregate recovery in combination with aggregate associated OM on a chronosequence of reclaimed surface mine sites and a native, undisturbed reference site. Macroaggregate and micro-within-macroaggregate proportions increased with reclamation age, while microaggregate proportions decreased. Organic carbon (C) and total nitrogen (N) concentrations increased with reclamation age for each aggregate fraction and were higher in the OM fraction observed within soil aggregates than in the free OM fraction found between soil aggregates. Naturally occurring isotopic signatures of ¹³C decreased rapidly with reclamation age, indicating over 50% of total aggregate C to be new C from predominately C₃ plant community inputs after 26 years of reclamation. Soil aggregate size distribution trends of increasing macroaggregation and micro-within-macroaggregates along with rapid rates of OM accumulation with time indicated that reclaimed soils had recovered structurally towards a native soil condition after a period of 10-15 years.     

炼油污水生物滤池深度处理中试试验研究

根据废水特性和回用水质要求,分析了废水回用在技术和经济上的可行性,并结合抚顺石化分公司石油一厂的废水处理特点,确定了浮选—生物滤池—臭氧催化氧化—快滤(FBOF)工艺的污水处理回用方案,并进行中试试验。结果表明:污水经该工艺路线处理后,出水水质的各项指标均大大低于循环冷却水补水的国家标准,完全能够满足回用要求。     

离心速度与时间对奶牛隐孢子虫卵囊浮集效果的影响

采用饱和糖溶液漂浮法,选择不同离心速度(1000,1500,2000,2500,3000,3500r/min)与不同离心时间(6,9,12,15,18,21.24,27min)对同一隐孢子虫阳性牛粪卵囊浮集效果作了比较观察,F检验及多重比较.结果表明,在3000r/min转速条件下离心21min时卵囊浮集效果明显高于其它各组,此即为分离牛隐孢子虫卵囊较为理想的离心速度和离心时间.     

针对受污染水源的水处理流程改造

介绍周口市二水厂针对微污染原水所作的技改实例。该实例将现有的虹吸滤池改为气浮式虹吸滤池，使水处理流程由混凝──沉淀──过滤变为混凝──沉淀──气浮──过滤，从而强化了水处理系统的整体性能及其对原水水质的适应能力。