Phostrip除磷系统生物特性及工艺研究

本研究采用 Phostrip 除磷系统,对于低有机物浓度的城市污水,即使在外界气温0℃左右,进水温度约11℃时,系统有机物 COD 平均去除率可达78.9%,T—P 平均去除率可达87.3%,出水 T—P 可保持在1mg/L 以下,Phostrip 工艺运行稳定,有机物及磷的去除效果较好。工艺运行受进水负荷波动及温度变化的影响很小,特别对解决低温低有机物浓度城市污水的生物除磷是较理想的工艺系统。     

前置厌氧池DAT-IAT的工艺特性试验

试验采用前置厌氧池的DAT-IAT工艺方法,以城市污水为处理对象研究工艺的生物降解过程及除磷效果。试验结果表明:该工艺处理城市污水能获得很好的处理效果且工艺稳定性高。IAT池曝气4hCODCr平均去除率可达到97.6%;氨氮的去除率因受进水氨氮负荷影响使得变化范围较大,从53.3%到98.7%,平均去除率在90%以上;厌氧池的设置使总磷的去除效果尤为突出,平均去除率在90.0%以上。     

进出水方式对高负荷浅层渗滤净化生活污水效果的影响

为研究农村分散住户用水不均匀和排放泵井运行不连续条件下高负荷地下浅层渗滤系统的净化效果,建立渗滤试验柱,以实际生活污水为进水,在12.5 cm.d-1日均水力负荷下,比较连续进水、间歇进水和自由排水、间歇排水对实际生活污水净化效果的影响。结果表明,各渗滤柱对NH4+-N的平均去除率均大于96%。对COD的平均去除率为41.2%～67.7%,其中采用间歇进水、间歇排水方式的渗滤柱去除率最低,但出水仍可达到GB8978—1996《污水综合排放标准》中二级标准。各渗滤柱对TN的平均去除率为17.5%～37.2%,其中采用间歇进水、间歇排水的渗滤柱平均去除率最高,表明强化反硝化作用是提高脱氮效率的主要途径。对TP的平均去除率为51.0%～78.0%,其中采用连续进水、间歇排水的渗滤柱平均去除率最高,表明延长污水停留时间、增加与填料的接触面积能增强对TP的去除效果。间歇进水、间歇排水方式下,渗滤柱对COD的去除效果有所下降,但是对N、P营养盐的综合去除效果最好。     

垂直潜流人工湿地净化北方微污染水体试验研究

为研究垂直潜流人工湿地对北方微污染水体中COD、氮和磷的去除效果及去除机理,在室内选用混合土(由炉渣与种植土按比例混合而成)、石英砂和陶粒作为填料,以天津当地常见植物黄花鸢尾为植被构建了垂直潜流人工湿地处理微污染景观湖水和雨季的初期雨水;除冬季冰封期暂停运行外,通过对系统不同季节运行数据的分析,考察了不同季节环境条件下垂直潜流人工湿地对我国北方城市微污染水体的净化效果及影响因素。结果表明:不同季节条件下,该系统对污染物均有着良好的去除效果和抗冲击负荷能力。微污染景观水和雨季初期雨水经垂直潜流人工湿地系统处理后,出水COD、NH4+-N及TP的质量浓度可分别优于GB 3838—2002《地表水环境质量标准》的IV类、III类和II类水质标准(研究阶段进水TP≤0.80 mg·L-1),COD、NH4+-N和TP的阶段平均去除率最高可分别达80%、91%和82%;TN的去除效果受季节变化波动较大,阶段平均去除率在32%~78%,温度较低季节或原水水质较差时有待处理水回流或辅加其他技术手段以提高脱氮效果。垂直潜流人工湿地对北方微污染水体有着较好的净化效果,能够有效地预防地表水体富营养化的发生,有利于城市水环境质量的改善和水资源的循环利用,具有良好的发展应用前景。     

矿化垃圾湿地处理畜禽养殖废水的研究

采用序批式进水方式,在m(固)∶V(液)=1∶20及水力负荷1.25 m3.m-2.d-1条件下,研究种植旱伞草(Cyperus alternifolius)、芦苇(Phragmites australis)、美人蕉(Canna indica)和菖蒲(Acorus calamus)4种植物的矿化垃圾填料湿地对畜禽养殖废水的处理效果。持续运行90 d的结果表明,矿化垃圾填料湿地床对CODCr、SS、NH4+-N和TP的平均去除率分别为41.3%～52.5%、55.2%～72.1%4、4.2%～76.7%和40.1%～68.0%。不同植物种类对去除率的影响小,与无植物空白相比约有10百分点的变化,主要被矿化垃圾填料自身特性所掩盖。矿化垃圾填料硝化能力强,导致硝酸盐氮(NO3--N)的累积高达数十mg.L-1,并导致TN去除率偏低,仅为41.6%～45.9%。构建了150 cm高的矿化垃圾填料柱进行反硝化脱氮,在水力负荷0.30 m3.m-2.d-1条件下运行90 d期间内,距柱面120 cm处NO3--N去除率在ρ(NO3--N)约为20和40 mg.L-1的水质条件下均可达97%以上。     

微曝气生物滤池-固相碳源反硝化生物滤池强化脱氮处理新运粮河水的示范工程研究

滇池是中国富营养化状态最为严重的湖泊,而入湖河流氮磷元素的输入是其主要原因。河流水质的低C/N特征是限制氮素去除的关键因素,采用固相反硝化技术能够为反硝化过程提供持续的碳源,因而能够强化受污染河流的脱氮效果。以滇池的重点控制入湖河流-新运粮河为研究对象,设计了微曝气生物滤池(Biological aerating filter,BAF)-固相碳源反硝化(Solid-phase denitrification,SPD)组合工艺,在河道旁路展开示范工程研究。组合工艺设计规模为800 m3·d-1,BAF(气水比为3∶1~5∶1)和SPD生物滤池的最大表面水力负荷分别为4.2和1.4 m3·m-2·h-1,其中SPD生物滤池采用新型固相碳源共混可生物降解聚合物与惰性载体共混作为生物膜载体。工艺研究结果表明,在BAF气水比为3∶1~5∶1、HRT为0.5~1 h和SPD滤池HRT为0.5~1 h的运行工况下,BAF对NH4+-N的平均硝化率达到了91.27%,SPD滤池的平均反硝化率93.60%,工艺出水NH4+-N、NO3--N和NO2--N平均浓度分别为0.68、0.70和0.02 mg·L-1。示范工程对各项污染物的去除效果良好,对TN、TP和CODCr的去除率分别达到84.93%、50.15%和31.39%;工艺出水TN、TP和CODCr平均浓度分别为1.75、0.20和22.96 mg·L-1,主要水质指标均达到了地表水V类水质标准。采用新型固相碳源填充的反硝化生物滤池强化了工艺针对低C/N水质特征污染水体的脱氮效果,组合工艺对滇池氮素输入控制具有重要的意义。     

潜流人工湿地低温下黄河原水预处理效果研究

在低温条件下(水温0.3～15.9℃),采用水平潜流人工湿地在玉清湖水库进水口处对入库黄河水进行预处理试验研究,考察了低温下黄河原水预处理效果,比较了不同水力负荷条件下,湿地系统对污染物的去除效率及其变化趋势,同时考察了进水污染物含量的影响.结果表明:在运行期间,潜流人工湿地有较好的处理效果,COD、TP、TN、NH4 -N的平均去除率均分别达到43.13%、40.86%、42.56%、43.26%.根据GB3838-2002<地表水环境质量标准>,出水中COD达到Ⅰ类,TP平均值达到Ⅱ类,TN平均值达到Ⅴ类;NH4 -N平均值达到Ⅱ类.处理效果与温度正相关,在现有的水力负荷变化范围内(0.6 ～1.2 m·d-1),系统处理效果无明显差别.同时发现,由于本实验的进水负荷低,系统去除功能未能得到充分利用,今后的研究可以适当提高负荷,充分利用系统的净化能力.     

人工增氧型复合湿地污染物净化效果

针对传统人工湿地负荷低、硝化能力弱和易堵塞的缺点,结合曝气生物滤池与人工湿地强化理论的研究成果,自主开发了人工增氧型复合湿地工艺,即生物接触氧化预处理+微曝气垂直流湿地+水平潜流湿地。通过对滇池北岸城郊混合制污水处理的模型试验,分析该工艺流程各净化单元的污染物去除效果。结果显示,人工增氧型复合湿地对不同水力负荷和污染负荷都体现了较强的缓冲调节能力和较高的净化效果。对污染物的总去除率分别为SS 94.5%、CODCr71.3%、氨氮72.3%,在进水总氮10.0 mg.L-1条件下实现了41.9%的总氮去除率,出水总氮均值为5.8 mg.L-1。     

人工快速渗滤法处理小城镇污水的模拟试验研究

小城镇污水既是水资源的主要污染源,同时也是可利用水资源的重要组成部分,高效率、低成本的小城镇污水处理技术是农业生态安全和工程节水的急需。研究采用人工快速渗滤方法处理小城镇污水,在湿干比一定（湿干比1∶3）的条件下设3种填料比[V（土）∶V（砂）=1∶1、2∶1和3∶1）和3种不同水力负荷周期[短周期（0.5 d进水,1.5 d落干）、中周期（1 d进水,3 d落干）和长周期（3 d进水,9 d落干）]进行交叉试验。跟踪测定处理后水中COD、总磷、凯氏氮和铵氮的去除率。结果表明,系统的COD和总磷去除效果较好,最高去除率分别达到73.19%和54.86%。COD的去除受水力负荷周期影响较大,在长水力负荷周期条件下去除效率高,总磷的去除受水力负荷周期的影响小。系统对凯氏氮和铵氮的去除效率偏低,两者的最高去除率分别为46.67%和40.67%,均在长周期条件下取得。     

活性污泥-悬浮生物膜系统处理低C/N污水深度脱氮性能

通过农业废弃物玉米芯悬浮生长生物膜的载体,构建了活性污泥-悬浮生物膜混合系统,以SBR工艺运行方式对低浓度低C/N污水的深度脱氮性能进行了研究.探究了挂膜启动阶段系统脱氮效果;在工艺稳定运行后,考察了温度、HRT、DO、进水C/N、进水pH等参数对工艺脱氮性能的影响.经过24 d挂膜后,结合污染物去除情况及镜检显示生物膜挂膜成功.运行结果表明,以预处理后的生活污水作为模拟原水,控制反应温度为26—30℃,HRT=8 h,COD/TN为(4.0±0.1),DO=(2.2±0.1) mg·L^-1,进水pH=(8.0±0.1)的条件下,系统达到最佳运行条件,COD、NH₄⁺-N、TN平均去除率分别为70.2%、94.8%和80.8%,平均出水COD、NH₄⁺-N、TN浓度分别为14.89 mg·L^-1、0.57 mg·L^-1和2.40 mg·L^-1.好氧阶段DO浓度对TN去除率有一定的影响,当好氧阶段DO浓度为(2.2...     

人工湿地系统对含沼液畜禽废水净化效果试验研究

为了考察人工湿地处理含沼液畜禽废水的可行性,采用水平潜流人工湿地对含沼液畜禽废水进行处理实验。试验结果表明：在进水流量1.5 m3.d-1,水平潜流人工湿地系统对含沼液畜禽废水具有较好的处理效果。废水中COD、TP、TN和NH4＋-N浊度平均去除率分别为59.21%、53.80%、55.09%和55.57%.另外,通过对人工湿地沿程的污染物变化试验分析表明,人工湿地系统对污染物的降解是沿人工湿地水流方向逐渐降低的。     

扰动对水体富营养化的改善作用

利用人工构建的模拟水体系统,观察搅拌和曝气条件下水体中氮磷含量和形态的变化规律,研究和探讨了扰动对水体富营养化的改善。结果表明：（1）扰动对上覆水体氮的去除效果不明显,但是能够有效促进底泥中氨氮向水体扩散,从而使底泥中氮含量明显降低,运行99 d后,曝气反应器中底泥总氮含量从初始3.46 g.kg-1降至0.68 g.kg-1,仅为对照反应器的1/4;（2）搅拌对上覆水中磷的去除效果最佳,反应器运行期间,总磷的平均去除率为37%左右;（3）扰动能增加底泥中微生物的数量和多样性,为污染物的生物降解提供了良好的基础。合理运用扰动能够提高水中溶解氧含量,改善微生态环境,增加微生物的数量和种类,有利于水体富营养化的改善。     

A/O-MBR处理某经济区市政污水的效能

采用A/O-MBR法处理某经济区市政污水,对其进、出水的水质进行连续监测,考察系统稳定性和处理效果。结果表明,在水力停留时间12小时,污泥龄30天,回流比75%,好氧段DO浓度1.3～8.5 mg/L的条件下,系统对COD、氨氮、总氮、总磷的平均去除率分别为92.04%、93.66%、78.04%、91.06%。反硝化...     

Optimization of phosphorus removal in uniFed SBR system for domestic wastewater treatment

The characteristic of phosphorus removal and appropriate change of the traditional operation modes were investigated in UniFed sequencing batch reactor (SBR) laboratory-scale apparatus (40 L), treating actual domestic wastewater with low ratios of C/N (2.57) and C/P (30.18), providing theoretical basis for actual application of wastewater treatment plant. UniFed SBR system with its unique operation mode had the distinct superiority of phosphorus removal. On this occasion, the effect of volumetric exchange ratio (VER) and the method of influent introduction for phosphorus removal were studied. When the carbon source became the limiting factor to phosphorus release, the higher the VER, the lower the phosphorus concentration in the effluent. Three different influent patterns, including one-time filling, four-time filling, and continuous filling with the same quantity of wastewater could increase the release rate of anaerobic phosphorus from 0.082 to 0.143 mg·P·(L·min)^-1. Appropriate change of the traditional operation modes could optimize the efficiency of phosphorus removal. When the feed/ decant time was extended from 2 h to 4 h, the phosphorous removal efficiency increased from 59.93% to 88.45% without any external carbon source. In the mode of alternation of anoxic-aerobic (A/O) condition, phosphorous removal efficiency increased from 55.07% to 72.27% clearly. The carbon source in the influent can be used adequately, and denitrifying phosphorus removal was carried out in anoxic stage 2 (A2). This mode was optimal for the treatment of actual domestic wastewater with low C/N and C/P ratios.     

Process evaluation of an alternating aerobic-anoxic process applied in a sequencing batch reactor for nitrogen removal

In order to improve the nitrogen removal efficiency and save operational cost, the feasibility of the alternating aerobic-anoxic process (AAA process) applied in a sequencing batch reactor (SBR) system for nitrogen removal was investigated. Under sufficient influent alkalinity, the AAA process did not have an advantage over one aerobicanoxic (OAA) cycle on treatment efficiency because microorganisms had an adaptive stage at the alternating aerobic-anoxic transition, which would prolong the total cycling time. On the contrary, the AAA process made the system control more complicated. Under deficient influent alkalinity, when compared to OAA, the AAA process improved treatment efficiency and effluent quality with NH₄ ⁺-N in the effluent below the detection limit. In the nitrification, the average stoichiometric ratio between alkalinity consumption and ammonia oxidation is calculated to be 7.07 mg CaCO₃/mg NH₄ ⁺-N. In the denitrification, the average stoichiometric ratio between alkalinity production and NO₃ ^?-N reduction is about 3.57 mg CaCO₃/mg NO₃ ^?-N. As a result, half of the alkalinity previously consumed during the aerobic nitrification was recovered during the subsequent anoxic denitrification period. That was why the higher treatment efficiency in the AAA process was achieved without the supplement of bicarbonate alkalinity. If the lack of alkalinity in the influent was less than 1/3 of that needed, there is no need for external alkalinity addition and treatment efficiency was the same as that under sufficient influent alkalinity. Even if the lack of alkalinity in the influent was more than 1/3 of that needed, the AAA process was an optimal strategy because it reduced the external alkalinity addition and saved on operational cost.     

湖滨带复合型人工湿地氮磷的去除效果

湖滨带是连接湖泊水域生态系统与陆地生态系统的一个功能过渡区,是湖泊的最后一道保护屏障。在河流的入湖口建造湖滨湿地,可有效净化入湖径流中携带的部分有机污染物、营养盐等。以云南抚仙湖北岸的湖滨湿地—马料河复合人工湿地为研究对象,探讨了湿地不同功能区去除氮磷的效果。研究表明,沉淀池除氮效果最不明显,在该区内有机氮可能发生矿化作用而转变为氨氮。有植物系统的潜流和表流区除氮效果较为明显,潜流区对氨氮、硝氮和总氮的平均去除率分别达18.0%、19.7%和22.6%;表流区对三者的平均去除率分别达50.4%、35.9%和43.5%。沉淀池对磷有一定的截留作用,且在进水污染物质量浓度较高时表现明显,平均截留率为14.9%。潜流和表流区除磷效果不明显,可能是因为湿地运行了两年多,土壤吸附交换达到平衡,影响了表流区的除磷效果。潜流区除磷效果受降雨影响较大,雨季时,总磷的平均截留率为12.1%,主要是不溶性磷的吸附和沉积;雨季末期,湿地流量较小,水体流动性差,系统内处于厌氧状态,出现磷释放现象。     

土壤渗滤系统中污染物去除效果分析

在土壤渗滤系统中,水力负荷、有机负荷和碳氮比等因素均对营养盐的处理效率具有显著影响.在实验室控温条件下,分析了不同水力负荷、有机负荷和环境条件对土壤渗滤系统污染物去除效果的影响.结果表明,在水力负荷小于0.15 m3·m^-2·d^-1的条件下,模拟生活污水中CODCr、总氮和总磷去除率分别达到84％、37％和93％以上,土壤（以干土计）亚硝酸盐细菌数量为4.50× 106 g^-1.装置上层产生的滞水对CODCr和磷酸盐的去除影响不大,但是由于处理系统内溶解氧浓度降低,使得氨氮硝化过程受到抑制,氨氮和总氮的处理效果均变差;在通气良好条件下,较高的碳氮比[m（碳）：m（氮）=5：1]对系统中总氮的去除更为有利.     

几种植物对潜流型湖滨湿地中氮磷的处理效果比较

湖滨带是连接湖泊水域生态系统与陆地生态系统的一个功能过渡区,是湖泊的最后一道保护屏障。在河流的入湖口建造湖滨湿地,可有效净化入湖水中携带的部分有机污染物、营养盐等。湿地净化污染物的机理极为复杂,其中植被起着重要的作用。选择适当的植物是构建湿地系统的关键。以云南省抚仙湖北岸的湖滨湿地——马料河潜流型湿地为研究对象,探讨了美人蕉(Cannaindica),菖蒲(AcoruscalamusLinn),伞竹(Cyperusalternifolius),香蒲(Typhaelatifolia)四种不同植被系统的潜流型湖滨湿地去除污水中营养盐的效果,为抚仙湖湖滨带人工湿地的合理优化选择植物提供一定的依据。结果表明,四种植被系统的潜流湿地对总氮和总磷均有一定的去除效果。但是由于湿地长期运行而疏于管理,植物没有定期收割翻新,四种植物的氮磷去除率差别不太大,去除效果均不太佳。其中,美人蕉对总氮和总磷的去除效果较好,其去除率分别是30.4%,19.13%,其次为香蒲和伞竹,效果较差的是菖蒲。并且实验表明,暴雨对四种植物湿地氮的去除效果有很大的影响。连续几天的暴雨情况下,四种植物系统氮的去除率都很低。     

Advanced nitrogen removal by pulsed sequencing batch reactors (SBR) with real-time control

The feasibility of pH and oxidation reduction potential (ORP) as on-line control parameters to advance nitrogen removal in pulsed sequencing batch reactors (SBR) was evaluated. The pulsed SBR, a novel operational mode of SBR, was utilized to treat real municipal wastewater accompanied with adding ethanol as external carbon source. It was observed that the bending-point (apex and knee) of pH and ORP profiles can be used to control denitrification process at a low influent C/N ratio while dpH/dt can be used to control the nitrification and denitrification process at a high influent C/N ratio. The experimental results demonstrated that the effluent total nitrogen can be reduced to lower than 2 mg/L, and the average total nitrogen (TN) removal efficiency was higher than 98% by using real-time controll strategy.     

Research on polyhydroxyalkanoates and glycogen transformations: Key aspects to biologic nitrogen and phosphorus removal in low dissolved oxygen systems

In this paper, a study was conducted on the effect of polyhydroxyalkanoates (PHA) and glycogen transformations on biologic nitrogen and phosphorus removal in low dissolved oxygen (DO) systems. Two laboratory-scale sequencing batch reactors (SBR1 and SBR2) were operating with anaerobic/aerobic (low DO, 0.15–0.45 mg·L^-1) configurations, which cultured a propionic to acetic acid ratio (molar carbon ratio) of 1.0 and 2.0, respectively. Fewer poly-3-hydroxybutyrate (PHB), total PHA, and glycogen transformations were observed with the increase of propionic/acetic acid, along with more poly-3-hydroxyvalerate (PHV) and poly-3-hydroxy-2-methyvalerate (PH2MV) shifts. The total nitrogen (TN) removal efficiency was 68% and 82% in SBR1 and SBR2, respectively. In the two SBRs, the soluble ortho-phosphate (SOP) removal efficiency was 94% and 99%, and the average sludge polyphosphate (poly-P) content (g·g-MLVSS^-1) was 8.3% and 10.2%, respectively. Thus, the propionic to acetic acid ratio of the influent greatly influenced the PHA form and quantity, glycogen transformation, and poly-P contained in activated sludge and further determined TN and SOP removal efficiency. Moreover, significant correlations between the SOP removal rate and the (PHV+ PH2MV)/PHA ratio were observed (R²>0.99). Accordingly, PHA and glycogen transformations should be taken into account as key components for optimizing anaerobic/aerobic (low DO) biologic nitrogen and phosphorus removal systems.