共查询到20条相似文献,搜索用时 500 毫秒
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生物接触氧化法是以生物膜净化废水的处理工艺。该法具有处理时间短、氧化效率高、节省构筑物体积、运行管理方便等优点。一般接触氧化法都采用波纹板、塑料蜂窝、玻璃钢蜂窝等硬性填料。由于硬性填料价格昂贵、使用不当易发生填料堵塞等问题,接触氧化法在应用上受到了一定的局限。因此寻求价廉易得、经久耐用、不易堵塞的新型填料成为接触氧化法迫切需要解决的问题。为探讨软性填料在毛纺染色废水中的应用,从1980年,北京清河毛纺织厂、北京纺织科学研究所、纺织部设计院开展协作,在北京清河毛纺织厂进行了“软性填料生物接触氧化法处理毛纺染色废水”的试验研究工作。在试验研究过程中,先后进行了对不同纤维填料的筛选、涤纶纤维填料不同结构型式的选择 相似文献
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蔡明初 《石油化工环境保护》1981,(6)
一、原理与发展简况生物滤池是圆或方形的筒状构筑物,内装各种填料,使微生物生长在填料表面。处理的废水自上而下流动时,通常由于废水温度较气温高,池内空气受废水喷淋而温度升高。这样池内外气温不同,产生压差导致空气向上流动,空气就不断从池底部自动进入从池顶排出。 相似文献
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实验针对间歇投配污水的生物渗滤池处理生活废水的一些基本运行参数进行了优化研究。通过对生物渗滤池的出水量、不同填料性质、不同填料粒径以及不同进水水质与污染物(COD)去除率影响的研究,证实该系统的水力负荷与污染物去除率成反向关系,即当水力负荷减少时,污染物去除率会相对增加;研究还表明选用粒径为0.9~2mm自然河沙作为系统填料时,系统COD去除率较高,这时填料不易被堵塞且即使堵塞也较易恢复;运用生物渗滤池处理城市生活污水能使处理后污水COD达到城镇污水处理厂出水排放标准的一级标准。提高污水中营养物质的配比以及采用多级生物渗滤池联用,能高效处理高浓度污水,甚至使出水达标排放。 相似文献
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采用厌氧生物法处理了人工合成的焦化废水,试验表明:三种浓度的合成焦化废水(COD值分别为1500、3000及7500mg/L)可被有效地降解,去除率可达80%以上。在厌氧反应器内填软性填料后,焦化废水中对厌氧微生物具有抑制作用的邻甲酚、间甲酚可部分被吸附在生物膜上,使其抑制作用显著降低。 相似文献
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AF+BAF用于处理树脂化工集中区废水厂尾水的研究 总被引:1,自引:1,他引:0
采用厌氧滤池(AF)+曝气生物滤池(BAF)工艺处理树脂化工废水,曝气生物滤池以陶粒为生物载体,进水COD为200~300 mg·L-1,实验规模均为2~4 L·d-1.实验表明,采用AF+BAF工艺对化工园区尾水有较好的处理效果,在AF停留24h,BAF停留12 h的条件下,COD的去除率最高可达73.4%,NH+4-N的去除率达到93.8%.通过气相色谱-有机质谱联用仪(GC-MS)和三维荧光光谱分析发现,系统对小分子有机物和微生物代谢产物的去除显著,但对饱和烷烃和含氮杂环类物质去除效果不佳.变性梯度凝胶电泳(DGGE)谱图显示,AF中的微生物种类比原废水厂上流式厌氧池(UASB)中更为丰富,表明化工园区废水采用二次厌氧效果明显. 相似文献
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以苯、联苯和萘为模型化合物,研究了厌氧滤池(AF)反应器在反硝化及连续运行条件下对含这几种芳香族化合物模拟废水的处理效果,并以葡萄糖为补充碳源,考察了不同C/N对有机物反硝化降解特性的影响.结果表明,在长期连续流运行及反硝化条件下,AF反应器对废水中几种典型芳香族化合物具有良好地去除效果,当进水COD浓度约为1?000mg/L,苯、联苯和萘总浓度为60mg/L时,出水COD去除率可达到90%,芳香族化合物的去除率可达到84%.苯比萘和联苯更易于反硝化降解.C/N在5~30范围内,苯的降解率均达到90%,C/N对苯的降解没有明显影响;COD、萘和联苯去除率受C/N影响较大,C/N为15时,COD、萘和联苯去除率最大,分别为90%、78%和82%. 相似文献
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In order to investigate the oxygen tolerance capacity of upflow anaerobic solid-state(UASS)with anaerobic filter(AF) system, the effect of microaeration on thermophilic anaerobic digestion of maize straw was investigated under batch conditions and in the UASS with AF system. Aeration intensities of 0–431 m L O2/gvswere conducted as pretreatment under batch conditions. Aeration pretreatment obviously enhanced anaerobic digestion and an aeration intensity of 431 m L O2/gvsincreased the methane yield by 82.2%. Aeration intensities of 0–355 m L O2/gvswere conducted in the process liquor circulation of the UASS with AF system. Dissolved oxygen(DO) of UASS and AF reactors kept around 1.39 ±0.27 and 0.99 ± 0.38 mg/L, respectively. p H was relatively stable around 7.11 ± 0.04. Volatile fatty acids and soluble chemical oxygen demand concentration in UASS reactor were higher than those in AF reactor. Methane yield of the whole system was almost stable at 85 ± 7 m L/gvs as aeration intensity increased step by step. The UASS with AF system showed good oxygen tolerance capacity. 相似文献
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在市政污水处理厂进行同步厌氧氨氧化反硝化(SAD)工艺小试.以A/O除磷和亚硝化工艺处理后的生活污水为基质,启动厌氧氨氧化滤柱.反应器启动成功后,基质中分别投加葡萄糖和丙酸钠启动SAD工艺.结果表明,常温条件(13~22℃)下,进水投加30 mg·L~(-1)葡萄糖,SAD工艺耦合效果良好,平均出水总氮浓度为6.41 mg·L~(-1).相较于厌氧氨氧化工艺,SAD工艺出水总氮浓度降低了42%;低温环境(10~13℃)中,投加30 mg·L~(-1)葡萄糖,SAD工艺稳定性受到破坏并向反硝化工艺转变;常低温环境(10~22℃)中,基质中投加30 mg·L~(-1)丙酸钠,SAD工艺均有良好的处理效果,平均出水总氮浓度为6.54mg·L~(-1),丙酸钠对低温SAD工艺影响较小. 相似文献
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深床过滤颗粒截留机理研究 总被引:4,自引:0,他引:4
对深床过滤过程中颗粒物与滤料之间的相互作用进行了理论分析,讨论了两者间的相互作用及影响因素对微絮凝深床过滤进行了中试研究,考察了1~l0μm粒径颗粒在500cm滤床中的截留情况,并连续65h监测滤柱水头损失的变化;在滤速为24m/h情况下,计算了1~10μm粒径颗粒所受的水流剪切力;利用理论分析,分别讨论了表面电位为-25mV及-125mV、粒径为1~10μm的颗粒与滤料之间的物理化学作用力.理论计算值对实验结果进行了很好的解释,说明可以通过颗粒与滤料间的作用力分析来研究均质滤料深床过滤运行规律. 相似文献
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An advanced anaerobic biofilter (AF) was introduced for the treatment of coal gasification wastewater (CGW), and effluent recirculation was adopted to enhance phenol removal and methane production. The results indicated that AF was reliable in treating diluted CGW, while its efficiency and stability were seriously reduced when directly treating raw CGW. However, its performance could be greatly enhanced by effluent recirculation. Under optimal effluent recirculation of 0.5 to the influent, concentrations of chemical oxygen demand (COD) and total phenol in the effluent could reach as low as 234.0 and 14.2 mg/L, respectively. Also, the rate of methane production reached 169.0 mL CH4/L/day. Though CGW seemed to restrain the growth of anaerobic microorganisms, especially methanogens, the inhibition was temporary and reversible, and anaerobic bacteria presented strong tolerance. The activities of methanogens cultivated in CGW could quickly recover on feeding with glucose wastewater (GW). However, the adaptability of anaerobic bacteria to the CGW was very poor and the activity of methanogens could not be improved by long-term domestication. By analysis using the Haldane model, it was further confirmed that high effluent recirculation could result in high activity for hydrolytic bacteria and substrate affinity for toxic matters, but only suitable effluent recirculation could result in high methanogenic activity. 相似文献
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生物除磷机理及试验研究 总被引:7,自引:1,他引:7
介绍了生物除磷机理、生物除磷系统的积磷细菌、生物除磷所需的环境条件。SBR法除磷的试验研究表明,应用SBR活性污泥系统进行除磷,需要一定的厌氧条件;且须在厌氧阶段进行充足的曝气。试验结果证明,SBR法在时间上控制的灵活性非常适合生物除磷的环境条件。厌氧与好氧相结合,能够提高磷的去除率或降低出水磷的浓度,磷的去除率可达90%左右。 相似文献
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Two runs of experiments were carried out to obtain an understanding of phosphorus release and uptake under the anaerobic condition and then the aerobic condition respectively. Under anaerobic condition, it was found that the extent of phosphorus release appeared to increase with the increase of the initial organic loading rate when the initial organic loading rate was up to 0. 1 gSCOD/gMLSS.When the initial organic loading rate was higher than 0. 1 gSCOD/gMLSS, the amount of phosphorus release per unit mass of MLSS reached heady a same stationary value, and it seemed this is not affected by organic loading rate when there is extemal available substrate remained. In addition, the effect of NOx-N on the phosphorus release and uptake was also investigated, it was proved that the denitrifiers has an advantage over polyphosphate accumulating bacteria in competition for organic substrate under anoxic condition. Therefore, the existence of NOx-N is disadvantageous to the phosphorus release. Based upon the above investigations, the process configuration of membrane bioreactor(MBR) in combination with anaerobic phase was proposed to enhance the removal of phosphorus in treating domestic wastewater. Dunng the experimental period of four months, average removals of 92.50%, 84.25%, 100%, 94.09% and 85.33% were achieved for COD, TP, SS, NH3-N and TN respectively. 相似文献