循环流化床锅炉脱硫效率分析及监测实例

分析总结了循环流化床（CFB）锅炉的脱硫机理以及影响其脱硫效率的各种因素,对某燃煤热电厂和某生物质环保热电厂的循环流化床锅炉脱硫效果（加石灰石前后二氧化硫的排放情况）进行了实测,结果表明：采用循环流化床添加石灰石炉内脱硫后的烟气排放完全满足中国相关排放标准的要求。通过加强对循环流化床锅炉运行的管理,可具有广阔的应用前景。     

厌氧膨胀颗粒床（EGSB）反应器在有机废水治理中的研究进展

厌氧膨胀颗粒床（EGSB）反应器作为第三代高效厌氧反应器代表工艺之一,它通过增大反应器的高径比和采用出水回流技术,使反应器内的水力上升流速远远高于UASB反应器,强化了传质效果,提高了处理效率。适用于超高浓度和含有毒物质的工业废水,也特别适用于低温低浓度有机废水的处理。还展望了EGSB反应器未来的发展前景。     

曝气生物滤池在印染废水处理中的应用

采用曝气生物滤池工艺处理印染废水的二级生化出水。废水COD浓度从进水90～140mg/L降到80mg/L以下,色度从32倍降到16倍以下,排放水质稳定达到广东省《水污染排放限值DB44/26-2001》第一时段一级标准。通过近半年的试验表明,曝气生物滤池工艺具有占地面积少、运行稳定、成本低、出水水质好等优点,在印染废水后段深度处理中有重要的作用。     

高级氧化-BAF深度处理焦化废水

采用O3+BAF和Fenton+BAF两种工艺去除焦化废水中经生物处理后的残余污染物,考察了O3浓度、pH值、亚铁/双氧水配比、双氧水加入量、曝气时间等影响因素。结果表明,当臭氧加入量为800mg/L,BAF曝气时间为18h,双氧水加入量为0.5mL/L,亚铁为2g/L,出水COD都低于70mg/L,色度低于50倍,达到一级排放标准。     

生物流化床法处理污泥回流液的影响因素研究

将生物流化床工艺与活性污泥工艺相结合,以市政污水处理厂污泥回流液为研究对像。以0.3～0.45mm活性炭颗粒为载体对生物流化床中微生物进行培养、驯化,挂膜成功后,分别对生物流化床厌氧段和好氧段进行了单因素试验,得出进水的最佳pH值介于7.0～7.5,生物流化床厌氧段的最佳水力停留时间4.4h、最佳碳源为蔗糖,;缺氧段及好氧段的最佳水力停留时间2.69h、8.06h,曝气量0.5mL/min。在最佳工艺参数条件下进行污泥回流液脱氮除磷试验得出,此工艺可使总氮浓度为150.0mg/L,总磷浓度为59.0mg/L的污泥回流液的总氮浓度降低至65.19mg/L,此时的总氮去除率为56.54%;总磷的去除率较低。试验结果表明,该工艺对处理污泥回流液中氮磷具有一定的效果。     

从废水中回收沼气能及氢能与电能

厌氧发酵制沼气、厌氧发酵制氢和微生物燃料电池技术是利用微生物在废水处理的同时回收能源的三种主要方式。文章结合相关研究现状,介绍了这三种技术的基本原理及其在废水处理领域的发展状况和展望,并对三种生物能源进行了比较。     

循环流化床干法脱硫除尘一体化工艺去除汞探讨研究

目前,由于人类污染源每年向大气排汞量日益增长,使国际上对汞排放的控制研究成为热点,本文通过理论计算及工程实例说明了循环流化床干法烟气脱硫除尘一体化工艺系统可以有效地控制燃煤电厂汞的排放。     

疾病预防控制中心废水处理技术工程实例

疾病预防控制机构废水具有重金属种类繁多、含病原体数量大、间断性排放等特点,通过运用混凝沉淀＋曝气生物滤池（BIOFOR）＋ClO2消毒工艺对其废水进行处理,处理后废水达到《医疗机构水污染物排放标准（》GB18466-2005）排放标准。     

Influence of temperature on the characteristics of aerobic granulation in sequencing batch airlift reactors

Aerobic granular sludge was cultivated in sequencing batch airlift reactors(SBAR) at 25,30,and 35°C,respectively.The effect of temperature on the granules characteristics was analyzed and the microbial community structures of the granules were probed using scanning electron microscope(SEM) and polymerase chain reaction-denaturing gradient gel electrophoresis(PCR-DGGE).The results showed that 30°C is optimum for matured granule cultivation,where the granules had a more compact structure,better settling abili...     

Effectiveness of fluidized pellet bed for removing soluble contaminants

Fluidized pellet bed (FPB) has been successfully applied in water and wastewater treatment. However, the removal mechanism of contaminants especially the soluble ones, is still unclear. This study aimed to evaluate the e ectiveness of FPB reactor for removing soluble contaminants from synthetic wastewater. By only coagulation through jar test operation with addition of polyaluminium chloride (PACl) as primary coagulant and polyacryamide (PAM) as coagulant-aid, the removals of soluble chemical oxygen demand (COD), total phosphorus (TP), and NH4 +-N were found to be only 2.2%–7.5%, 5.7%–25.5%, and 9.9%–18.5%, respectively. However, by FPB operation under the same dosage of coagulants, these values increased to 82.7%, 37.2%, and 50%, indicating that the formation of pellets in the FPB e ectively enhanced the removal of soluble contaminants. By careful comparison of the settleablility and filterability of the pollutants after coagulation, the originally soluble contaminants could be divided into three groups, namely: (1) coagulated-andsettleable, (2) coagulated-but-nonsettleable, and (3) uncoagulable. It was found that not only the first two groups but also a large part of the third group could be e ectively removed by FPB operation. However, the mechanism for the removal of the uncoagulable pollutants by FPB operation still needs further investigation.