共查询到19条相似文献,搜索用时 78 毫秒
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实验采用改良型CAST工艺,考察了不同诱导模式下系统的除磷脱氮性能.结果表明,在缺氧条件下投加亚硝酸盐对系统反硝化除磷性能的抑制作用较大,投加量为5 mg·L~(-1)时系统除磷性能变差.相比较,好氧投加亚硝酸盐的CAST系统更稳定,当亚硝酸盐投加浓度为5、10、15 mg·L~(-1)时各工况初期除磷性能均有小幅波动,但分别经过10、6、34 d驯化后,除磷率迅速回升并稳定在95%以上,出水磷浓度均小于0.5 mg·L~(-1);投加量为20 mg·L~(-1)时工艺除磷性能急速恶化,但污泥的亚硝酸盐型缺氧吸磷能力是驯化前的10.4倍,说明投加一定浓度亚硝酸盐导致的除磷性能恶化可以解除,且长期投加有利于富集以NO_2~-为电子受体的反硝化聚磷菌.实验还发现,好氧投加一定浓度亚硝酸盐系统污泥沉降性能良好且污泥浓度不断降低,这对污泥减量具有一定指导意义. 相似文献
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探究ABR-MBR耦合工艺在无污泥回流及在ABR各隔室接种高浓度(25g·L-1,以MLSS计)活性污泥条件下启动反硝化除磷性能的可行性以及反硝化除磷隔室内微生物群落特征.结果表明,通过逐步提升硝化液回流比(R)由0%至200%成功启动反硝化除磷性能.稳定运行过程中,系统对COD、 PO3-4-P和TN的平均去除率分别为88.28%、 54.45%和61.93%.在ABR进水容积负荷(以COD计,下同)为0.8 kg·(m3·d)-1、R为150%、 ABR和MBR的水力停留时间(HRT)分别为9h和3.3 h时,VFA平均产量为80.58mg·L-1、回流硝化液的ρ(NO-2-N)/ρ(NO-3-N)平均为1.68,PO3-4-P和TN的平均去除率分别为64.94%和62.95%,实现短程硝化和反硝化除磷耦合.批次实验证明反... 相似文献
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采用序批式污泥培养方式,探讨了NO2-为电子受体的反硝化除磷工艺特征.结果表明,通过逐步增加进水中NO2-浓度并取代NO3-,可有效驯化反硝化聚磷菌(DPAO)对较高浓度NO2-(以N计,30mg/L)的有效利用.DPAO可根据电子受体的变化作出动态响应,进而影响系统的除磷效能.在NO3-条件下,系统中存在2 类DPAO:DPAO35(以NO2-或NO3-为电子受体)和DPAO5(以NO3-为电子受体);作为系统的优势功菌,DPAO 占总VSS 的40%~61%.随着进水中NO3-的减少和NO2-的增加,DPAO5 被缓慢淘洗出系统,DPAO 比例减少为28%~41%,同时引起聚糖菌(GAO)比例从31%~52%升至54%~67%,而除磷效率从84%降至66%.化学计量学显示厌氧8710;Gly/8710;HAc 和好氧8710;Gly/8710;PHA 比值(C/C)分别由0.53 和0.43 升至0.78 和0.51. 相似文献
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MUCT-MBR工艺反硝化除磷脱氮研究 总被引:3,自引:2,他引:1
自行设计的双反应器MUCT-MBR简化了MUCT工艺,将反应池由5个简化到2个,减小了工艺占地面积,并且采用膜过滤取代二沉池出水,操作简单,出水安全可靠.针对MUCT-MBR工艺脱氮除磷性能,尤其是反硝化除磷功能进行研究.结果表明,当进水C/N/P比在33.3/5/1~25/5.5/1范围内,整个实验过程中COD、 TN和TP平均去除率分别达到89.3%、 75.4%、 79.2%;且膜出水不受污泥沉降性的影响.缺氧段的反硝化吸磷是MUCT-MBR工艺除磷的关键,系统运行至第58 d,系统中反硝化除磷菌(DPAOs)所占比例达84.2%,反硝化除磷占系统总磷去除的67.07%. 相似文献
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反硝化除磷作为一种新型可持续发展技术受到广泛关注. 前期在多级缺氧-好氧工艺的基础上开发了一种新型反硝化除磷工艺(DPR-MAO). 为探明内循环系统对DPR-MAO工艺脱氮除磷效能的影响,考察了不同内循环比条件下的氮磷去除效果,分析了各反应池的脱氮除磷过程以及微生物群落特征. 结果表明:当内循环比由100%提至200%时,总氮和总磷的平均去除率由76.05%和86.39%分别提至87.46%和93.42%. 通过氮磷质量平衡分析发现,提高内循环比可以使工艺表现出优良的反硝化除磷性能. 高通量测序结果表明,DPR-MAO工艺中具有反硝化除磷功能的菌属主要有Thiothrix、Dokdonella、Candidatus accumulibacter、Thauera、Comamonas、Dechloromonas和Pseudomonas. 当内循环比由100%提至200%时,具有反硝化除磷功能的菌属的相对丰度总和增加了约4倍,其中Thiothrix的相对丰度由0.36%~0.52%增至53.58%~56.64%. 研究显示,提高内循环比可以强化DPR-MAO工艺的反硝化除磷效果以及反硝化聚磷菌在微生物群落中的优势地位. 相似文献
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电子受体亚硝酸氮在反硝化除磷过程中的作用 总被引:5,自引:0,他引:5
针对先前文献提到的亚硝酸氮在反硝化除磷中存在着一定的抑制作用,以亚硝酸氮作为电子受体,对其在缺氧反硝化吸磷过程中的抑制影响进行了大量的静态烧杯试验.结果表明,在亚硝酸氮浓度大于30mg·L-1的时候,确实存在严重的抑制作用,而且该临界抑制浓度与污泥的特性和运行操作条件等因素有关;但是在亚硝酸氮浓度低于25mg·L-1的情况下不会对反硝化条件下磷的吸收产生毒害作用,相反地,它可以取代氧气、硝酸氮做为良好的电子受体用来进行缺氧段磷的生物摄取,在反硝化除磷中表现一定的积极作用. 相似文献
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Wang Yayi Wang Shuying Peng Yongzhen Zhu Guibing Ling Yunfang 《Frontiers of Environmental Science & Engineering in China》2007,1(2):226-232
To supply the valuable operating parameters for the popular usage of the new denitrifying phosphors removal process, it is
essential to study the dominant biochemical reactions and the characteristics of denitrifying phosphorus removing bacteria
(DPB). Thus, parallel batch experiments using DPB sludge were carried out to assess the effect of substrates (sewage, HAc,
and endogenous carbon source) on denitrifying dephosphorus removal efficiency in this study. The results showed that the initial
specific phosphorus release rate increased with the high concentration of the short-chain volatile fatty acids ratio in the
influent, and sufficient phosphorus was released by DPB. This improved the subsequent denitrification and phosphorus uptake
efficiency. The specific endogenous denitrification mainly relies on the internal carbon source (PHB) stored by poly-P bacteria.
Denitrifying phosphorus removing bacteria were very hungry when the internal PHB was consumed. Consequently, the specific
endogenous denitrification rate was low and the phosphorus uptake did not happen. On the other hand, in the experiment, the
denitrifying phosphorus removal performance under two temperature conditions (8–10°C and 25–26°C) was also investigated and
analyzed. It was found that the lower temperature decreased the specific phosphorus release and uptake rate, but did not inhibit
the denitrifying phosphorus removal completely. Therefore, the negative influence of the low temperature on the overall phosphorus
removal was not significant.
Translated from Acta Scientiae Circumstantiae, 2006, 26 (2): 186–192 [译自: 环境科学学报] 相似文献
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为了提高系统的反硝化除磷脱氮效率,采用静态试验考察了厌氧反应时间和厌氧段COD对A2O-BAF工艺反硝化聚磷效果的影响,同时对缺氧阶段反硝化聚磷量与脱氮量之间的关系进行了探讨.试验结果发现,在试验范围内,随着厌氧反应时间和厌氧段COD的增加,厌氧释磷量均增加,反硝化聚磷量,净聚磷量和硝氮去除量亦都随之增加,但是反硝化聚磷量与释磷量的比值基本维持不变.在2组8个不同的试验条件下,缺氧段反硝化聚磷量和脱氮量之间均呈现出良好的线性关系,系数为1.007~1.053,R2为0.992~0.997,反映了A2O-BAF系统中污泥的固有特性. 相似文献
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Experimental study of nitrite accumulation in predenitrification biological nitrogen removal process
Xuelei Wu Lunqiang Chen Yongzhen Peng Yayi Wang Pu Wang 《Frontiers of Environmental Science & Engineering in China》2008,2(2):236-240
The effect of dissolved oxygen (DO) concentration on nitrite accumulation was investigated in a pilot-scale pre-denitrification
process at room temperature for 100 days. In the first 10 days, due to the instability of the system, the DO concentration
fluctuated between 1.0 and 2.0 mg/L. In the next 14 days, the DO concentration was kept at 0.5 mg/L and nitrite accumulation
occurred, with the average nitrite accumulation rate at 91%. From the 25th day, the DO concentration was increased to 2.0
mg/L to destroy the nitrite accumulation, but nitrite accumulation rate was still as high as 90%. From the 38th day the nitrite
accumulation rate decreased to 15%–30% linearly. From the 50th day, DO concentration was decreased to 0.5 mg/L to resume nitrite
accumulation. Until the 83rd day the nitrite accumulation rate began to increase to 80%. Dissolved oxygen was the main cause
of nitrite accumulation, taking into account other factors such as pH, free ammonia concentration, temperature, and sludge
retention time. Because of the different affinity for oxygen between nitrite oxidizing bacteria and ammonia oxidizing bacteria
when DO concentration was kept at 0.5 mg/L, nitrite accumulation occurred.
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Translated from Environmental Science, 2006, 27(12): 2472–2476 [译自: 环境科学] 相似文献
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厌氧-好氧-缺氧短程硝化同步反硝化除磷工艺研究 总被引:4,自引:0,他引:4
构建了主要由厌氧-好氧-缺氧构成的短程硝化同步反硝化除磷工艺,并在常温条件下用于生活污水的处理.研究发现,通过调节反应器内好氧区的pH(8.2~8.7)和溶解氧(DO为3~5mg·L-1)能实现该工艺的快速启动,在好氧区内实现亚硝酸盐的累积.在稳定运行期内,DO是影响短程硝化的主要影响因素,好氧1区DO控制在1.5~2.0mg·L-1,好氧2区DO控制在0.5~1.0mg·L-1,好氧区内亚硝酸盐氮累积浓度稳定在5~10mg·L-1,氨氮去除率达到90%以上.各反应单元内碳源、硝酸盐和亚硝酸盐对除磷贡献的研究表明,该工艺的缺氧段实现了在不外加碳源的情况下以亚硝酸盐和硝酸盐共同作为电子受体的反硝化除磷,反硝化除磷量占系统总除磷量的80%以上. 相似文献
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采用厌氧/缺氧/好氧和生物接触氧化反应器(A2/O-BCO)组成的反硝化除磷系统处理模拟生活污水,通过调节进水乙酸钠、丙酸钠的配比(乙酸钠:丙酸钠分别为1:0,2:1,1:1,1:2和0:1),考察了系统对有机物的去除以及同步脱氮除磷的影响,同时通过高通量测序对比了不同配比下微生物菌群结构的变化.结果表明:乙酸钠丙酸钠配比对有机物和NH4+-N的去除影响较小,对厌氧段有机物的消耗和TN的去除率以及磷的释放和吸收影响较为明显;TP去除率仅为50.3%~56.8%,需进一步优化系统的运行参数.当乙酸钠:丙酸钠=1:1时,厌氧段有机物消耗量最大,占有机物流入量的61.2%,厌氧释磷量最大(23.2mg/L)且缺氧吸磷率最高(71.4%),而TN的去除效果则随丙酸钠含量的增加而增加.高通量测序结果表明:A2/O反应器中微生物多样性降低,混合碳源污泥中微生物多样性比单一碳源更丰富;驯化后的污泥中绿弯菌(Chloroflexi)和螺旋菌(Saccharibacteria)减少,变形菌(Proteobacteria)和拟杆菌(Bacteroidetes)增加.BCO反应器中Nitrospira和Nitrosomonas总占比为2.1%~31.4%,且抑制亚硝酸盐氧化菌(NOB)的活性,有利于短程硝化的实现. 相似文献
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Yuan Linjiang Han Wei Wang Lei Yang Yongzhe Wang Zhiying 《Frontiers of Environmental Science & Engineering in China》2007,1(1):23-27
In order to achieve simultaneous nitrogen and phosphorus removal in the biological treatment process, denitrifying phosphorus
accumulation (DNPA) and its affecting factors were studied in a sequencing batch reactor (SBR) with synthetic wastewater.
The results showed that when acetate was used as the sole carbon resource in the influent, the sludge acclimatized under anaerobic/aerobic
operation had good phosphorus removal ability. Denitrifying phosphorus accumulation was observed soon when fed with nitrate
instead of aeration following the anaerobic stage, which is a vital premise to DNPA. If DNPA sludge is fed with nitrate prior
to the anaerobic stage, the DNPA would weaken or even disappear. At the high concentration of nitrate fed in the anoxic stage,
the longer anoxic time needed, the better the DNPA was. Induced DNPA did not disappear even though an aerobic stage followed
the anoxic stage, but the shorter the aerobic stage lasted, the higher the proportions of phosphorus removal via DNPA to total
removal.
Translated from Environmental Science, 2004, 25(6): 92–96 [译自: 环境科学] 相似文献
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温度对生物强化除磷工艺反硝化除磷效果的影响 总被引:7,自引:1,他引:7
以处理城市污水的中试规模生物强化除磷A2/O活性污泥工艺系统为研究对象,考察了温度对系统COD去除和脱氮除磷效果的影响,特别是温度对活性污泥反硝化除磷性能的影响.结果表明,当温度从(30.9±0.8)℃降低到(9.1±0.6)℃时,A2/O系统的脱氮除磷效果显著下降,系统对TN和TP的污泥去除负荷明显下降.通过污泥反硝化除磷活性实验发现,随着温度的降低,系统中活性污泥的最大厌氧释磷速率、最大好氧吸磷速率和最大缺氧吸磷速率都降低.活性污泥中反硝化除磷菌(DPB)占聚磷菌(PAOs)总量的比例随温度降低稍有下降,但平均值仍维持在47.5%左右.用阿伦尼乌斯公式对实验结果进行拟合,得到系统中活性污泥聚磷菌厌氧释磷反应活化能Ea1为148.0 kJ· mol-1,聚磷菌好氧吸磷反应活化能Ea2为228.8 kJ·mol-1,发生在缺氧条件下反硝化除磷菌的吸磷反应活化能Ea3为315.8 kJ·mol-1.对不同温度下污泥絮体粒径分析结果表明,随温度降低,粒径分布更加集中,系统中活性污泥絮体颗粒平均粒径减小,不利于污泥絮体内部反硝化除磷缺氧微环境的形成. 相似文献