共查询到18条相似文献,搜索用时 187 毫秒
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错流式膜-生物反应器处理生活污水及其生物学研究 总被引:11,自引:5,他引:6
用错流式膜-生物反应器(CrosflowMembraneBioReactor简称CMBR)进行处理生活污水试验并研究其生物动力学参数.结果表明:当HRT为5h,SRT为15d,膜面流速为4m/s,膜通量为75、150L/(m2·h)时,CMBR处理生活污水试验的去除率为:COD>97%、NH3-N>97%、浊度≥98%;对SS和总E.coli则达到100%,出水水质优于建设部生活杂用水回用标准CJ25.1-89.生物相分析表明,污泥中没有原、后生动物,只有菌胶团.推导了CMBR稳态运行时的生物浓度计算公式,进而求得表观产率因数Yg为0.65,衰减常数Kd为0.1d-1. 相似文献
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超滤膜-生物反应器处理生活污水及其水力学研究 总被引:25,自引:3,他引:22
用超滤膜-生物反应器进行处理生活污水试验并研究其水力学行为。结果表明,当HRT为5h、SRT为30d、膜面流速为4m/s膜流量为75L/(m^2·h)时,试验出水水质优于建设部生活杂用水水质标准CJ25.1-89,可直接回用。 相似文献
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采用UBF反应器在中温35℃对蛋鸡场鸡粪混合液离心出水进行处理,试验结果表明,在进水CODCR为19500mg/L,NH3-N为1800mg/L的条件下,水力停留时间为24.85h,容积负荷为18.84KCODCr/m^3.d时〉CIODCr去除率为80.28%,BOD3去除率为89.65%,产气率为0.558m^3/去除KgCODCr,反应器运行状态良好。 相似文献
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厌氧-水解反应器稳定运行的试验研究 总被引:11,自引:1,他引:11
采用造纸废水对厌氧水-水解反应器的启动、运行进行试验研究。结果表明,当MLVSS在15g/L左右,COD容积负荷为1.45kg/(m^3·d),水力负荷为2.0m^3/(m^2·h),水国停留时间为4h,污泥颗粒化程度较高,反应器运行效果稳定可靠。 相似文献
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厌氧氨氧化微生物颗粒化及其脱氮性能的研究 总被引:22,自引:4,他引:18
利用厌氧颗粒污泥作为种泥,启动SBR反应器,旨在培养厌氧氨氧化颗粒污泥以及研究其脱氮性能.结果表明,水力停留时间(HRT)是富集厌氧氨氧化微生物的1个重要控制因素,以HRT为30 d,第58 d时,SBR反应器就出现厌氧氨氧化现象,与此同时,颗粒污泥由灰黑色变为棕褐色,粒径减小.到第90 d时,成功培养出厌氧氨氧化颗粒污泥,NH+4-N和NO-2-N同时被去除,最大去除速率分别达到14.6 g/(m3·d)和6.67 g/(m3·d).从第110 d开始,逐步降低HRT,以提高基质负荷促进厌氧氨氧化菌生长.到目前t=156 d,HRT降到5 d,氨氮和亚硝酸氮的去除率分别达到60.6%和62.5%,亚硝酸氮/氨氮的比率为1.12.污泥也由棕褐色变为红棕色,形成红棕色的具有高厌氧氨氧化活性颗粒污泥,总氮负荷达到34.3 g/(m3·d). 相似文献
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蠕虫在膜生物反应器和活性污泥法中的污泥减量研究 总被引:10,自引:0,他引:10
通过长达345d的中试规模试验,研究比较了蠕虫在膜生物反应器(MBR)和活性污泥法(CAS)的生长状况及其导致的污泥减量效果.CAS中的蠕虫生长状况明显优于MBR的蠕虫生长状况.MBR曝气池中平均蠕虫密度(10条·mg-1)远低于CAS曝气池中平均蠕虫密度(71条·mg-1),并且CAS中蠕虫连续保持高密度(>30条·mg-1)生长达172d.CAS中红斑瓢体虫和仙女虫交替成为优势蠕虫.蠕虫生长对MBR的污泥产率(0 40kg·kg-1)和污泥沉降性能(污泥沉降指数133mL·g-1)影响很小,但却能显著减少CAS的污泥产率(0 17kg·kg-1)和改善污泥沉降性能(污泥沉降指数为60mL·g-1).仙女虫比红斑瓢体虫能更大地减少污泥产量和更好地改善污泥沉降性能.蠕虫生长不影响MBR的COD去除率和出水水质,但却显著影响CAS的COD去除率和出水水质. 相似文献
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Fu Xu Zhenxing Huang Hengfeng Miao Hongyan Ren Mingxing Zhao Wenquan Ruan 《环境科学学报(英文版)》2013,25(10):2031-2040
Two identical full-scale biogas-lift reactors treating brewery wastewater were inoculated with different types of sludge to compare their operational conditions, sludge characteristics, and kinetic models at a mesophilic temperature. One reactor (R1) started up with anaerobic granular sludge in 12 weeks and obtained a continuously average organic loading rate (OLR) of 7.4 kg chemical oxygen demand (COD)/(m3.day), COD removal efficiency of 80%, and effluent COD of 450 mg/L. The other reactor (R2) started up with residual activated sludge in 30 weeks and granulation accomplished when the reactor reached an average OLR of 8.3 kg COD/(m^3·day), COD removal efficiency of 90%, and effluent COD of 240 mg/L. Differences in sludge characteristics,biogas compositions, and biogas- lift processes may be accounted for the superior efficiency of the treatment performance of R2 over R1. Grau second-order and modified StoverKincannon models based on influent and effluent concentrations as well as hydraulic retention time were successfully used to develop kinetic parameters of the experimental data with high correlation coefficients (R2 〉 0.95), which further showed that R2 had higher treatment performance than R1. These results demonstrated that residual activated sludge could be used effectively instead of anaerobic granular sludge despite the need for a longer time. 相似文献
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一体式膜生物反应器污水资源化技术研究 总被引:3,自引:1,他引:3
膜生物反应器是高效的污水处理工艺,但其高气水比运行条件产生的动力消耗与国外膜组件昂贵的价格成为膜生物反应器在我国应用的主要限制因素。为此本研究采用分体曝气形式,选择国产高抗污性能PVDF中空纤维膜,设计了间歇式膜生物反应器,研究了污泥浓度、曝气量和水力停留时间对一体式膜生物反应器去除污染物效果的影响。在低气水比条件下,MBR处理生活污水的研究表明,出水COD<50mg/L,BOD<10mg/L,NH3—N<20mg/L,浊度<3NTU,悬浮固体浓度为零,优于生活杂用水水质标准(CJ25.1-89)。 相似文献
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Kwang Ho Ahn Kwang Soo Kim Sung Won Kang Chul Yong Um Won Tae Lee Kwang Baik Ko 《环境科学学报(英文版)》2013,25(2):280-286
We evaluated the settling ability and dewaterability of granulated methane-oxidizing bacteria (GMOB) after granulation using a continuous-flow reactor. A comparative analysis on settling and dewatering characteristics due to changes in sludge retention time (SRT, 10, 15 and 20 days) during cultivation of GMOB was conducted. In assessing dewaterability, the specific resistance to filtration (SRF) of activated sludge and GMOB was found to be 8.21×1013-2.38×1014 and 4.88 × 1012-1.98×1013 m/kg, respectively. It was confirmed that as SRT decreased, SRF of GMOB increased. In the case of bound extracellular polymeric substance (EPS), activated sludge registered 147.5 mg/g-VSS while GMOB exhibited 171-177.2 mg/g-VSS. In the case of extracellular polymeric substance soluble EPS in effluent, activated sludge measured 62 mg/L and GMOB had 17.4-21.4 mg/L. The particle size analysis showed that mean particle diameters of GMOB were 402, 369, and 350 μm, respectively, at SRTs of 20, 15 and 10 days. In addition, it was found that GMOB had a larger mean particle diameter and exhibited much better settleability and dewaterability than activated sludge did. 相似文献
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研究一体化连续流间歇曝气膜生物反应器(IMBR)处理低C/N城市污水的工艺效能.试验结果表明:反应器在曝气2 h、搅拌2 h的运行模式下,对COD、NH_4~+;-N、TN和SS的平均去除率分别达到了87%,83.4%,75.4%和97.81%,各出水质量浓度平均值分别为17.5,4.59,7.63和2 mg/L,出水水质达到了GB/T18920-2002<城市污水再生利用城市杂用水水质>标准.Abstract: The integrated intermittent-aeration membrane biological reactor (IMBR) was investigated to treat the low C/N ratio urban sewage. Pollutants removal efficiency of IMBR under the condition of aeration 2 h and agitation 2 h were researched. The results showed that the average removal rates of COD, NH/ -N, TN and SS were 87% , 83.4% , 75.4% and 97.81% respectively. The average concentrations of COD,NH_4~+ -N,TN and SS in the effluent of IMBR system were 17.5,4.59,7.63 and 2 rag/L respectively. The effluent quality of IMBR could meet the standard of the requirement reclaimed water quality criterion (GB/T18920-2002). 相似文献
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Enhancing sewage sludge dewaterability by bioleaching approach with comparison to other physical and chemical conditioning methods 总被引:3,自引:0,他引:3
The sewage sludge conditioning process is critical to improve the sludge dewaterability prior to mechanical dewatering. Traditionally, sludge is conditioned by physical or chemical approaches, mostly with the addition of inorganic or organic chemicals. Here we report that bioleaching, an efficient and economical microbial method for the removal of sludge-borne heavy metals, also plays a significant role in enhancing sludge dewaterability. The effects of bioleaching and physical or chemical approaches on sludge dewaterability were compared. The conditioning result of bioleaching by Acidithiobacillus thiooxidans and Acidithiobacillus ferrooxidans on sludge dewatering was investigated and compared with the effects of hydrothermal (121℃ for 2 hr), microwave (1050 W for 50 sec), ultrasonic (250 W for 2 min), and chemical conditioning (24% ferric chloride and 68% calcium oxide; dry basis). The results show that the specific resistance to filtration (SRF) or capillary suction time (CST) of sludge is decreased by 93.1% or 74.1%, respectively, after fresh sludge is conditioned by bioleaching, which is similar to chemical conditioning treatment with ferric chloride and calcium oxide but much more effective than other conditioning approaches including hydrothermal, microwave, and ultrasonic conditioning. Furthermore, after sludge dewatering, bioleached sludge filtrate contains the lowest concentrations of chroma (18 times), COD (542 mg/L), total N (TN, 300 mg/L), NH4+-N (208 mg/L), and total P (TP, 2 mg/L) while the hydrothermal process resulted in the highest concentration of chroma (660 times), COD (18,155 mg/L), TN (472 mg/L), NH4+-N (381 mg/L), and TP (191 mg/L) among these selected conditioning methods. Moreover, unlike chemical conditioning, sludge bioleaching does not result in a significant reduction of organic matter, TN, and TP in the resulting dewatered sludge cake. Therefore, considering sludge dewaterability and the chemical properties of sludge filtrate and resulting dewatered sludge cakes, bioleaching has potential as an approach for improving sludge dewaterability and reducing the cost of subsequent reutilization or disposal of dewatered sludge. 相似文献
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The removal of biological nutrient from mature landfill leachate with a high nitrogen load by an internal circulation upflow sludge blanket (ICUSB) reactor was studied. The reactor is a set of anaerobic-anoxic-aerobic (A^2/O) bioreactors, developed on the basis of an expended granular sludge blanket (EGSB), granular sequencing batch reactor (GSBR) and intermittent cycle extended aeration system (ICEAS). Leachate was subjected to stripping by agitation process and poly ferric sulfate coagulation as a pretreatment process, in order to reduce both ammonia toxicity to microorganisms and the organic contents. The reactor was operated under three different operating systems, consisting of recycling sludge with air (A^2/O), recycling sludge without air (low oxygen) and a combination of both (A^2/O and low oxygen). The lowest effluent nutrient levels were realised by the combined system of A^2/O and low oxygen, which resulted in effluent of chemical oxygen demand (COD), NH3-N and biological oxygen demand (BOD5) concentrations of 98.20, 13.50 and 22.50 mg/L. The optimal operating conditions for the efficient removal of biological nutrient using the ICUSB reactor were examined to evaluate the influence of the parameters on its performance. The results showed that average removal efflciencies of COD and NH3- N of 96.49% and 99.39%, respectively were achieved under the condition of a hydraulic retention time of 12 hr, including 4 hr of pumping air into the reactor, with dissolved oxygen at an rate of 4 mg/L and an upflow velocity 2 m/hr. These combined processes were successfully employed and effectively decreased pollutant loading. 相似文献