盐雾试验方墨探讨

分析了不同盐雾试验方法标准对盐溶液配制、试样的处理和检测、试验参数、试验过程控制等方面的不同要求,探讨了盐雾试验的操作技术,提出了必须严格控制盐雾试验过程的建议和不能用不同标准进行的盐雾试验结果进行比较的观点.     

污水厂强化生物硝化和除磷的研究及运行策略

针对城镇污水厂运行过程中出现的问题(进水水质复杂、pH超标,造成NH3-N去除效率极低及某A/O工艺污水厂出水TP波动),进行了强化生物硝化和除磷的试验研究,得出了污水厂的运行控制策略,同时分析了A2/O工艺的运行模式对生物除磷的影响。     

SBR亚硝化快速启动过程中影响因子研究

在低DO条件下对SBR反应器实现快速亚硝化的途径及影响因素进行研究.控制反应器主要参数为：DO 0.15～0.40mg/L,pH值7.52～8.30,温度22.3～27.1℃,曝气时间为8 h.通过高、低氨氮浓度（245.28 mg/L与58.08 mg/L）交替进水的方式,经过57个周期（36 d）的稳定运行成功实现...     

序批式活性污泥法处理毛皮废水的研究

采用序批式活性污泥法处理毛皮模拟废水的试验条件为：水温２０℃,ＤＯ２ｍｇ／Ｌ,ＣＯＤｃｒ１５００ｍｇ／Ｌ,ＢＯＤ５ ９００ｍｇ／Ｌ,ＭＬＳＳ ２１００ｍｇ／Ｌ增至２６００ｍｇ／Ｌ左右,试验结果表明,采用限制曝气方式运行的序批式活性污泥系统最不易发生污泥膨胀。     

厌氧-好氧序列间歇式反应器处理生物制药废水的研究

采用厌氧序列间歇反应器与好氧序列间歇反应器相结合的技术,处理生物制药废水。结果表明,经7.0h厌氧搅拌处理和6.0h好氧曝气处理,进水COD为1180~3061mg/L,出水COD小于300mg/L,COD去除率在78.9%~92.8%之间,出水COD满足国家生物制药行业废水排放标准要求。      

AB法工艺在河东污水处理厂的应用

乌鲁木齐河东污水处理厂采用AB活性污泥工艺 ,设计处理污水 2 0× 10 4 m3 d ,于 1997年 7月投入运行 ,至今运行状况良好。本文介绍了该工程的工艺流程、设计参数、主要处理构筑物和运行情况 ,对运行中出现的问题进行了分析和探讨     

不同培养方式下兽疫链球菌发酵生产透明质酸的研究

对摇瓶的分批和补料、小罐的分批和流加发酵生产透明质酸（ＨＡ） 进行了比较研究,并对发酵机制进行了初步的探讨．在耗糖量相同的情况下,分批发酵比多次加料或流加发酵具有更高的ＨＡ产量和转化率;分批发酵初糖７％ ,发酵２４ ｈ 左右,产ＨＡ３．６ ｇ／Ｌ,转化率５．３ ％ ,流加发酵初糖３％ ,１５ ｈ 耗糖７％ ,此时,ＨＡ 为３ ．０ ｇ／Ｌ,转化率Ｙｐ／ｓ４．２％ ,继续发酵至２０ ｈ ,产ＨＡ４ ．０％ ,此时转化率Ｙｐ／ｓ３ ．６％ ,两种发酵所产ＨＡ 的Ｍｒ 均为２ ．０×１０６ ． 分批发酵中ＨＡ、副产物乳酸都和菌体生长相偶联,流加发酵中乳酸和菌体生长是偶联的,其含量均不断增加,ＨＡ含量表现为在菌体生长前期与之偶联,而后下降．流加发酵的菌体比生长速率远高于分批发酵．     

ASBR中强化活性污泥与普通活性污泥降解啤酒废水的对照研究

在厌氧序批式反应器(ASBR)中采用优势菌群对活性污泥进行强化,驯化出强化活性污泥。与普通活性污泥处理啤酒废水对照显示,强化活性污泥较普通厌氧污泥驯化成熟时间短,处理效果更稳定、更有效,CODcr去除率最高达95％。培育出的强化活性污泥颗粒粒径为1．5～2．5cm,较普通活性污泥颗粒粒径更大,更均匀。     

两级序批式MBR膜污染特性研究

采用两级SBR与膜法相结合的两级序批式MBR工艺处理生活污水,考察两级序批式运行模式对膜污染特性的影响.对运行111 d后的平板膜污染阻力分布进行了测算,并对两级序批式MBR与连续流单级好氧MBR的平板膜污染速率进行对比试验.结果表明: 两级序批式MBR的平板膜污染阻力以凝胶极化阻力为主,占总阻力的43%,沉积阻力较低,仅占总阻力的10%;与连续流单级好氧MBR相比,两级序批式MBR可以在更高的膜通量下运行,保持更低的膜污染速率,在运行42 d后,过膜流量从100 L/h下降至85 L/h,过膜压差从1.52×10~4 Pa增加至2.22×10~4 Pa;而连续流好氧MBR系统,过膜流量从61 L/h降低至39 L/h,过膜压差却从1.01×10~4 Pa增加至2.63×10~4 Pa.研究表明,两级序批式MBR工艺可以改善膜过滤过程的水力条件,从而有效地减缓浓差极化,降低沉积污染及凝胶层污染,序批式、膜间歇运行与空曝的结合起到了关键性作用.     

The formation of aerobic granular sludge for the treatment of real landfill leachate using a granular sequencing batch reactor at a constant volume

Leachate generated in a landfill may not be treated by conventional biological treatment due to its nature and complexity. The process of forming aerobic granules in batch sequencing reactors having features such as; reducing the settling process time and saving energy consumption and high decomposition rate have been noticed by researchers. In the present study, the structure of sequencing batch reactors (SBRs) was evaluated for the formation of granules, which were subsequently utilized for the treatment of landfill leachate. The experiment was initiated by using the GSBR, containing 1200 ml with different apparatuses, to develop granular sludge, and synthetic wastewater was added to reinforcement. The selected parameters for the operational hydraulic retention time (HRT) of the wastewater (6-h cycles) included feeding, idle, aeration, settling, and discharge. Furthermore, the controlled conditions were the dissolved oxygen (DO) range of 2–2.2 mg/L, temperature range of 20–23℃, and pH of 7.5–8.3. The chemical oxygen demand (COD), mixed liquor suspended solids (MLSS), and sludge volume index (SVI) daily were measured at the influent and effluent of GSBR reactor. The main properties of aerobic granular sludge were identified during the research procedures, and the remarkable settling and potent, high-density microbial structure of the granules were confirmed. The mean size of the formulated granules was estimated at 7.46 ± 1.8 mm, and the volume of the biomass also increased from approximately 1607 to 4137 mg/L through the granulation process. Moreover, 98% of the influent chemical oxygen demand (COD) could be removed by the formulated granular sludge, and the final-stage organic loading rate was estimated at 5.65 COD/m³/day. According to the results, GSBRs could be employed for the formulation of aerobic granular sludge for the treatment of landfill leachate.