三种反硝化滤池深度脱氮中试

以污水厂实际二级出水为处理目标,通过中试试验研究了陶粒滤料反硝化生物滤池、固定床反硝化砂滤池和连续过滤连续反冲砂滤池的特性。以甲醇作为外加碳源,3种滤池均可实现出水平均总氮小于5 mg/L。不足量投加外碳源会出现出水亚硝态氮的积累。当进水TN为15 mg/L左右时,为达到出水TN小于5 mg/L,生物滤池、固定床砂滤池和连续过滤砂滤池建议滤速分别为不大于8,5.2,6.2 m/h;滤池反硝化碳源投加比例分别为4.28,3.0,3.2 g甲醇/gTN;对应的反硝化容积负荷平均值分别为1.1,0.8,1.2 kg/(m3·d)。进水组分分析发现,有机氮不是出水总氮小于5 mg/L的限制因素。     

BAF-BAC工艺在炼油厂二级出水深度处理中的应用

采用曝气生物滤池-生物活性炭工艺对炼油厂二级处理出水的深度处理进行中试研究,拟探索炼油厂废水深度处理用于循环冷却水补水新工艺.结果表明,当进水COD浓度小于130mg/L,BAF滤速低于4.24m/h条件下运行时,该工艺平均出水COD浓度小于50mg/L,平均出水浊度为4.46NTU,同时对NH₄⁺-N也有一定的去除作用.     

Using a biological aerated filter to treat mixed water-borne volatile organic compounds and assessing its emissions

A biological aerated filter (BAF) was evaluated as a fixed-biofilm process to remove water-borne volatile organic compounds (VOCs) from a multiple layer ceramic capacitor (MLCC) manufacturing plant in southern Taiwan. The components of VOC were identified to be toluene, 1,2,4-trimethylbenzene, 1,3,5-trimethylbenzene, bromodichloromethane and isopropanol (IPA). The full-scale BAF was constructed of two separate reactors in series, respectively, using 10- and 15-cm diameter polypropylene balls as the packing materials and a successful preliminary bench-scale experiment was performed to feasibility. Experimental results show that the BAF removed over 90% chemical oxygen demand (COD) from the influent with (1188 605) mg/L of COD. A total organic loading of 2.76 kg biochemical oxygen demand (BOD)/(m3 packing d) was determined for the packed bed, in which the flow pattern approached that of a mixed flow. A limited VOC concentration of (0.97 0.29) ppmv (as methane) was emitted from the BAF system. Moreover, the emission rate of VOC was calculated using the proposed formula, based on an air-water mass equilibrium relationship, and compared to the simulated results obtained using the Water 9 model. Both estimation approaches of calculation and model simulation revealed that 0.1% IPA (0.0031–0.0037 kg/d) were aerated into a gaseous phase, and 30% to 40% (0.006–0.008 kg/d) of the toluene were aerated.     

反硝化滤池的数值模拟与模型校正

建立了反硝化滤池中试系统,在滤速8m/h,进水C/N分别为4和5两种工况条件下运行,考察其反硝化处理效果,结果表明在进水C/N=5条件下,出水TN浓度由14.52mg/L下降为7.14mg/L.应用BioWin软件,构建了反硝化滤池中试系统的模型,基于滤速8m/h,进水C/N=5条件下的运行数据,应用常规灵敏度分析法(Si,j)和均方根灵敏度分析法( ),对BioWin软件中的412个参数进行了灵敏度分析,结果表明,对反硝化滤池中试系统模拟结果影响最为显著的两类参数为:与甲基营养菌有关的计量学参数及与生物膜有关的参数.根据灵敏度分析结果,选取5个灵敏度最高的参数,通过调整参数值对所构建的反硝化滤池模型进行了校正,应用于滤速8m/h,进水C/N=5条件下的运行模拟取得了较好的效果.最后应用校正模型对滤速8m/h,进水C/N=4条件下的运行结果进行模拟,结果表明模拟值与实测值同样能够较好地吻合.由此得出结论,本研究所构建的反硝化滤池中试系统模型及基于灵敏度分析的模型校正方法是有效的,可用于实际反硝化滤池工艺的模拟.     

反硝化深床滤池海砂滤料截污特性研究

过滤功能作为反硝化深床滤池一项核心功能,为反硝化深床后置深度处理提供出水总悬浮物保证。为合理选配反硝化深床滤池海砂滤料,进行了两种反硝化深床滤池常用海砂滤料的满负荷进水穿透实验和连续进水过滤的实验。结果表明,在一定范围内提升反硝化深床滤池滤料粒径有助于降低流动相对滤料剪切力,有助于出水悬浮物达标。     

新型填料A/O生物滤池处理低碳氮比农村污水脱氮

针对低碳氮比导致低污染农村污水生物处理时出水总氮(total nitrogen, TN)质量浓度高不能满足排放标准的问题,以普通砾石A/O生物滤池为对照组(1号),采用芦竹和活性炭分别作为缺氧段和好氧段填料的A/O生物滤池(2号)处理人工模拟农村污水并研究其脱氮效果.结果表明,当进水化学需氧量(chemical oxygen demand, COD)、氨氮(ammonia nitrogen, NH⁺₄-N)和TN质量浓度分别为(79.47±14.21)、(34.49±2.08)和(34.73±3.87)mg·L^-1时,两套装置对COD、NH⁺₄-N和TN的去除率分别为(88.00±7.00)%和(89.00±10.00)%、(90.00±2.00)%和(97.00±7.00)%、(37±15)%和(68±7)%,表明添加新型填料芦竹和活性炭能显著增强A/O生物滤池对NH⁺₄-N和TN的去除.高通量测序结果显示, 1号装置中参与硝化过程...     

国内外灰水处理技术研究进展

生活污水分质收集与处理,尤其是对灰水的处理与回用可实现污水资源化利用,节约能源.介绍了生活污水分质收集基本概念和灰水水质、水量特点,重点对灰水处理技术如过滤、膜分离、MBR、人工湿地、生态滤池等的研究进展进行了综述,并对不同类型处理技术效果进行了对比分析.结果表明:单一的物理处理技术对有机物和表面活性剂等成分去除效果有...     

气水比对A/O-BF处理低碳氮比农村生活污水脱氮的影响

为揭示好氧段气水比对缺氧/好氧生物滤池(Anoxic/Oxic Biofilter,A/O-BF)脱氮的影响机理,采用A/O-BF处理低碳氮比农村生活污水,结合实时荧光定量聚合酶链式反应技术,对比研究了好氧段气水比为4∶1、2∶1和1∶1时A/O-BF的脱氮效能和微生物群落变化特征.结果表明:当气水比为4∶1时,A/O...