香根草和风车草人工湿地对猪场废水氮磷处理效果的研究

分别以香根草 (Vetiveriazizanioides )和风车草 (Cyperusalternifolius)为植被 ,按 1.0m× 0 .5m×0 .8m建立人工湿地 ,通过四季测试研究其对猪场废水N、P的净化功能及其随季节、进水浓度及水力停留时间变化的规律 .结果表明 ,两湿地对NH3 N和S PO3 -4 去除率受污水停留时间和污水浓度影响较大 .香根草或风车草人工湿地在春季对NH3 N和S PO3 -4 有明显的去除效果 ;在秋季 ,则对去除废水TN均有效果 ,在去除TP上 ,香根草湿地效果明显 ,风车草湿地效果差 .秋春季人工湿地随水力停留时间 (t)延长 ,TP或S PO3 -4 (Y)的去除遵从指数方程Yt=Y0 ·e-kt规律 .冬季和夏季 ,进水浓度对湿地去除P影响较大 ;在相同停留时间内 ,冬夏季人工湿地随进水浓度变化 ,进出水S PO3 -4 遵从直线方程 y =a +bx规律     

煤渣-草炭基质垂直流人工湿地系统对城市污水的净化效果

垂直流人工湿地系统不但具有较高的水力负荷率(54—64cm.^-1),而且对有机物和N、P都具有较高的去除效果．其对化粪池出水中的COD、BOD5、NIA4^+-N和总P的去除率分别为76％--87％,88％--92％,75％--85％和77％--91％．处理出水中COD、BOD5、NH4^+-N和总P的平均浓度分别小于60、20、25和2．0mg.L^-1.植物种植试验结果表明,种植风车草可提高氨氮、总N和总P的去除率,分别为2％--3％、4％--6％、10％--14％．     

红树植物人工湿地对生活污水的净化效果

研究了潜流型海桑（Sonneratia caseolaris）人工湿地、桐花树（Aegiceras corniculatum）人工湿地和木榄（Bruguiera gymnorrhiza）人工湿地对生活污水的净化效果。一年来,3种红树植物人工湿地对BOD5、CODCr、TP、TN、NH4^＋-N和NO2^--N的平均去除率分别达到83%、71%、41%、55%、50%和84%以上。人工湿地各处理周期之间,BOD5和CODCr去除率波动较小,而TP、TN、NH4^＋-N和NO2^--N去除率波动较大。3种红树植物人工湿地对各种污染物的净化效果存在一定的差异。海桑人工湿地和桐花树人工湿地对BOD5、CODCr、TP、TN和NH4^＋-N去除率明显高于木榄人工湿地,而海桑人工湿地和桐花树人工湿地相比较,除TP外,BOD5、CODCr、TN和NH4^＋-N去除率没有显著差异。人工湿地单一处理周期内,去除率随水力停留时间（HRT）的延长而增加。BOD5、CODCr、TN和NH4^＋-N在HRT为1d和2d的去除率分别为HRT为3d去除率的54%-65%和73%-84%,NO2^--N在HRT为1d和2d的去除率分别达到了HRT为3d的70%-81%和85%-94%,而TP在HRT为1d和2d的去除率分别只有HRT为3d的39%-50%和65%-74%。另外,红树植物人工湿地与风车草（Cyperus alternifoliu）人工湿地相比,前者的BOD5、CODCr、TP、TN和NH4^＋-N去除率明显小于后者（P〈0.05）。总体上看,3种红树植物人工湿地对生活污水的净化效果呈现海桑人工湿地≈桐花树人工湿地〉木榄人工湿地。     

潜流型菖蒲人工湿地不同C/N对污染物的去除效率

选取炉渣和砾石为基质,以无植被为对照,分别设置低、中、高浓度的3个碳水平(C1、C2、C3)和3个氮水平(N1、N2、N3)处理,研究潜流型菖蒲人工湿地在不同C/N下净化生活污水中COD、总氮(TN)、总磷(TP)的效果。结果表明,在不同C/N下,菖蒲人工湿地对污水中COD、TN的去除效果显著高于无植被的人工湿地,菖蒲植被能增加人工湿地COD去除率10.53%,增加TN去除率6.73%;而对于TP的去除,有无植被无显著差异。随着进水N、P浓度及C/N的变化,菖蒲湿地对COD、TN和TP的去除率分别为67.57%～75.85%、20.91%～56.82%和7.15%～17.78%;同时,菖蒲植株对N、P的积累量也相应的变化,其地上部的N、P积累量为4.44～14.79和1.11～3.37g.m-2,平均占湿地N、P去除率的6.91%和10.67%;地下部的N、P积累量分别为2.35～5.20和0.74～1.41g.m-2,平均占湿地N、P去除率的2.69%和6.02%。植物地上器官对湿地N、P的积累量大于地下部,有利于通过收割作用去除湿地系统中的N、P。     

风车草和香根草在人工湿地中迁移养分能力的比较研究

为研究风车草（Cyperus alternifolius）和香根草（Vetiveria zizanioides）迁移养分的能力,建立17.0 m²风车草潜流式人工湿地和13.3 m²香根草潜流式人工湿地处理猪场废水,在四个季节末测定植物生物量和组织氮、磷、铜、锌含量.结果表明,香根草地下部生物量大于风车草,地上部生物量则是风车草大于香根草.风车草年地上部收获量为3406.47 g·m^-2,比香根草的1483.88 g·m^-2高2.3倍;风车草的氮含量为22.69 mg·g^-1,比香根草的15.44 mg·g^-1高7.25 mg·g^-1;风车草的磷含量为6.09 mg·g^-1,比香根草的5.47 mg·g^-1高0.62 mg·g^-1.植株含铜、锌量风车草略比香根草高.风车草每年迁移N 68.72 g·m^-2和P 18.49 g·m^-2,香根草迁移N 8.93 g·m^-2和P 3.69 g·m^-2.风车草人工湿地每年由植物迁移的氮、磷、铜、锌比香根草高4～7倍.     

无土栽培美人蕉等植物处理生活废水的研究

采用无土栽培美人蕉、蕹菜、水稻、野生稻处理生活废水 .结果表明 ,静态试验中 COD、T- N、T- P等污染物的平均去除率 ,4种植物处理比对照分别高出 8.7～1 9.8%、2 0 .3～ 66.6%、2 3.5～ 61 .7% .4种植物对污染物的去除能力为美人蕉、蕹菜 >水稻 >野生稻 .3级植物塘系统中污染物去除率分别为 BOD2 79.7%、COD 71 .1 %、T- N66.5%、T- P 60 .7% ,而人工土快滤与植物塘的复合系统中则为 BOD583.9%、COD79.3%、T- N64.8%、T- P40 .9% .     

实验室模拟高负荷SPAC厌氧反应器运行

采用模拟废水, 对新型高负荷螺旋式自循环(Spiral automatic circulation, SPAC)厌氧反应器的运行性能进行了实验室模拟研究。结果表明: 在30oC, 水力停留时间(HRT)为12 h, 进水COD浓度从8000 mg/L升至20 000 mg/L的条件下, 反应器的COD去除率为91.1%~95.7%, 平均去除率为93.6％。在进水浓度为20 000 mg/L, HRT由5.95 h缩短至1.57 h的工况下, COD去除率从96.0%降低至78.7%, 反应器达到最高容积负荷率306 g COD/(L·d), 最大容积COD去除率240 g/(L·d), 最高容积产气率131 L/(L·d)。该反应器对基质浓度的连续提升具有良好的适应能力。进水COD浓度由8000 mg/L提升至20 000 mg/L时, 出水COD浓度一直处在较低水平(平均为852?mg/L), 容积COD去除率和容积产气率分别提高162%和119%。该反应器对HRT的连续缩短也有良好的适应能力。HRT由5.95 h缩短至1.57 h时,反应器容积COD去除率和容积产气率分别升高191%和195%。     

潜流人工湿地在城市污水三级处理中的应用

采用页岩/钢渣强化潜流人工湿地作为城市污水处理厂三级处理工艺.结果表明:在平均水力负荷为0.32 m·d-1的条件下,当进水有机物(CODcr)、总氮(TN)、总磷(TP)平均浓度为33.9、15.1和1.57 mg·L-1时,出水CODcr平均浓度为13.6 mg·L-1去除率为60%,面积速率常数KA值为0.3 m·d-1温度对CODcr的去除影响不明显;出水TN浓度在5.4～14.3 mg·L-1之间波动,KA值为0.09～0.31 m·d-1,去除率受温度的影响较大,随着进水硝态氮比例的提高和运行时间的延长,湿地对TN的去除效率有上升趋势;稳定阶段出水TP浓度为0.6 mg·L-1去除率为50%,KA为0.26 m·d-1温度对,TP去除影响不大.     

人工湿地对氮、磷的去除效率与动态特征

1999年1月~2003年12月对荣成人工湿地污水处理系统处理效果以及氮、磷去除效果的动态变化特征进行分析。结果表明,人工湿地对SS、COD、BOD均有很好的去除效果,出水浓度分别为27·8±6·7、91·0±13·7和23·8±4·6mg·L-1,去除率分别为71·8±8·4%、62·2±10·1%和70·4±9·6%。大肠菌群去除率为99·7%。对NH4+-N和TP去除效果较差,出水浓度分别为11·3±2·6和2·00±0·28mg·L-1,去除率分别为40·6±15·3%和29·6±12·8%。NH4+-N去除效果和季节变化有关,每年7~9月去除效果最佳,1~3月效果最差,去除率分别为50·7±12·4%和23·0±11·6%。TP的去除效果季节性变化不如NH4+-N明显。NH4+-N年平均去除率2001~2003年逐年增加。TP年平均去除率在2001和2002年基本相同,2003年有所降低。     

深型复合垂直流人工湿地对模拟污水处理厂尾水中PBDEs的去除研究

研究以四溴联苯醚(BDE-47)为目标污染物, 构建了两套深型复合垂直流人工湿地小试系统(IVCW, 总基质层高=180 cm)。在固定水力停留时间(HRT=3d)和水力负荷(0.3 m/d)条件下, 分析测定其对BDE-47(进水浓度=25 μg/L)的分段去除率, 并探讨PBDEs加入对IVCW系统常规净化效果与基质微生物的影响。批实验结果表明, 运行3个月后, IVCW对模拟污水中BDE-47去除率达到99.9%。与对照组相比, BDE-47处理组对氨氮的去除率由72.3%提高至82.9%, 但对硝态氮的去除率显著下降, 由53.0%降至28.1%, 化学需氧量(COD)去除率由88.1%降至82.3%。IVCW各单元基质中BDE-47的残留量沿水流方向逐渐递减, 在距离入流最近的下行流上层单元中BDE-47含量最高(约0.01 μg/g); 但BDE-47的加入导致基质微生物脱氢酶活性明显降低。微生物特征脂肪酸分析结果表明, 实验组与对照组下行流单元微生物群落组成差异明显, 分别以具有耐受型较强的微生物如革兰氏阳性厌氧菌和快速生长的好氧型革兰氏阴性菌为主。探究IVCW对BDE-47的去除潜力及迁移转化规律, 为生态工程系统应用于难降解有机污染物的治理提供有益参考和可行性方案。     

Treatment of tomato processing wastewater by an upflow anaerobic sludge blanket-anoxic-aerobic system

The main objective of this study is to assess the achievability of stringent discharge criteria i.e. BOD(5)<15 mg/L, TSS<15 mg/L and NH(4)-N<1mg/L during the treatment of tomato processing wastewater with COD of 2800-15,500 mg/L, BOD(5) of 1750-7950 mg/L, TKN of 48-340 mg/L and NH(4)-N of 21-235 mg/L. Two treatment systems, a UASB-aerobic system and a UASB-anoxic-aerobic system were tested. Furthermore due to alkalinity deficiency, in the raw wastewater, the study explored varying UASB effluent recirculation flowrates to the UASB influent to reduce additional alkalinity requirements. The UASB-anoxic-aerobic system was effective in treating tomato canning wastewater at an overall HRT of 1.75 days while achieving 98.5% BOD(5), 95.6% COD, 84% TSS and 99.5% NH(4)-N removal producing effluent BOD(5), COD, TSS, NH(4)-N, TKN, NO(2)-N, NO(3)-N and PO(4)-P of 10, 70, 15, 0.5, 3, 0, 60 and 4 mg/L, respectively. The biogas yield was 0.43 m(3)/kg COD removed.     

Seafood wastewater treatment in constructed wetland: tropical case

A series of investigations were conducted to evaluate the feasibility of using constructed wetlands to remove pollutants from seafood processing wastewater. Six emergent plant species; Cyperus involucratus, Canna siamensis, Heliconia spp., Hymenocallis littoralis, Typha augustifolia and Thalia deabata J. Fraser were planted in surface flow wetland. They were fed with seafood wastewater that was 50% diluted with treated seafood wastewater from an aerated lagoon. All macrophytes were found to meet satisfying treatment efficiency (standard criteria for discharged wastewater) at 5 days hydraulic retention time (HRT). While C. involucratus, T. deabata and T. augustifolia met acceptable treatment efficacy at 3 days HRT. Nutrient uptake rate of these species was observed in the range of 1.43-2.30 g Nitrogen/m(2)day and 0.17-0.29 g Phosphorus/m(2)day, respectively at 3 days HRT. The highest treatment performances were found at 5 days HRT. Average removal efficiencies were 91-99% for BOD(5), 52-90% for SS, 72-92% for TN and 72-77% for TP. Plant growth and nitrogen assimilation were experienced to be most satisfactory for C. involucratus, T. deabata and T. augustifolia. Lower HRTs affected contaminant removal efficiency for all species. C. involucratus, T. deabata and T. augustifolia can remove all contaminants efficiently even at the lowest hydraulic retention time (1 day).     

Some properties of a sequencing batch reactor system for removal of vat dyes

Bio-sludge from a wastewater treatment plant could be used as an adsorbent of vat dye from textile wastewater. Resting bio-sludge gave a higher adsorption capacity than dead bio-sludge. The resting bio-sludge from a textile wastewater treatment plant gave relatively high COD, BOD5 and dye adsorption capacity of 364.4 +/- 4.3, 178.0 +/- 9.0 and 50.5 +/- 1.3 mg/g of bio-sludge, respectively, in synthetic textile wastewater containing 40 mg/l Vat Yellow 1. Another advantage of the bio-sludge was that, after washing with 0.1 N NaOH solution, it was reusable without any activity loss. Through treatment with a sequencing batch reactor (SBR) system, both organic and dye in STIWW could be removed. The maximum dye (Vat Yellow 1), COD, BOD5 and TKN removal efficiencies of the SBR system under an MLSS of 2000 mg/l and an HRT of three days were 98.5 +/- 1.0%, 96.9 +/- 0.7%, 98.6 +/- 0.1% and 93.4 +/- 1.3%, respectively. Although, the dye and organic removal efficiencies of the SBR system with real textile wastewater were quite low, they could be increased by adding organic matters, especially glucose. The dye, COD, BOD5 and TKN removal efficiencies of the SBR system with glucose (0.89 g/l) supplemented textile industrial wastewater were 75.12 +/- 1.2%, 70.61 +/- 3.4%, 96.7 +/- 0.0%, and 63.2 +/- 1.1%, respectively.     

固定化微生物处理模拟污染地表水

以聚乙烯醇和海藻酸钠为包埋剂、驯化后的活性污泥为包埋菌剂,制备固定化微生物颗粒,其中包埋剂与包埋菌剂的比例为2:1。将该固定化微生物颗粒按20%的填充率装填到自制反应器中,用于处理模拟污染地表水,研究该固定化微生物的性能特点及其对模拟污染地表水的净化效果。结果表明:固定化微生物反应器的最佳水力停留时间为10h,最佳进水COD负荷为1.15～1.85g·L-1·d-1。在水温为20～29℃、溶解氧为3～4mg·L-1、水力停留时间为10h的条件下,当进水COD浓度为70.58～91.76mg·L-1、铵氮浓度为13.68～17.82mg·L-1时,COD去除率>62.3%,铵氮去除率>90.6%,表明固定化微生物能够有效地去除污染地表水中的COD和铵氮。     

UASB/Flash aeration enable complete treatment of municipal wastewater for reuse

A simple, efficient and cost-effective method for municipal wastewater treatment is examined in this paper. The municipal wastewater is treated using an upflow anaerobic sludge bed (UASB) reactor followed by flash aeration (FA) as the post-treatment, without implementing aerobic biological processes. The UASB reactor was operated without recycle, at hydraulic retention time (HRT) of 8 h and achieved consistent removal of BOD, COD and TSS of 60-70% for more than 12 months. The effect of FA on UASB effluent post-treatment was studied at different HRT (15, 30 and 60 min) and dissolved oxygen (DO) concentrations (low DO = 1-2 mg/L and high DO = 5-6 mg/L). The optimum conditions for BOD, COD and sulfide removal were 30-60 min HRT and high DO concentration inside the FA tank. The final effluent after clarification was characterized by BOD and COD values of 28-35 and 50-58 mg/L, respectively. Sulfides were removed by more than 80%, but the fecal coliform only by ~2 log. The UASB followed by FA is a simple and efficient process for municipal wastewater treatment, except for fecal coliform, enabling water and nutrients recycling to agriculture.     

Nutrient recovery from domestic wastewater using a UASB-duckweed ponds system

The pilot-scale wastewater treatment system used in this study comprised a 40-l UASB reactor (6-h HRT) followed by three duckweed ponds in series (total HRT 15 days). During the warm season, the treatment system achieved removal values of 93%, 96% and 91% for COD, BOD and TSS, respectively. Residual values of ammonia, TKN and total phosphorus were 0.41 mg N/l, 4.4 mg N/l and 1.11 mg P/l, with removal efficiencies of 98%, 85% and 78%, respectively. The system achieved 99.998% faecal coliform removal during the warm season with final effluent containing 4 x 10(3) cfu/100 ml. During the winter, the system was efficient in removing COD, BOD and TSS but not nutrients. The system was deficient in the removal of faecal coliforms during the winter, producing effluent with 4.7 x 10(5) cfu/100 ml. During the warm season, the N removal consisted of 80% by plant uptake, 5% by sedimentation and 15% unaccounted for. A duckweed production rate of 33 t dry matter per hectare per 8 months was achieved.     

Performance of a three-stage aerobic RBC reactor in food canning wastewater treatment

Biological treatment using attached growth in a three-stage lab-scale rotating biological contactor (RBC) was implemented for wastewater from food cannery industries. The wastewater contained high level of organic compounds due to fish and fruit cleaning, cooking and filling processes. Nutrients available in the wastewater enhanced the growth of microorganisms and allowed the biological treatment to be effective. The RBC consisted of 54 parallel discs rotating in a reservoir and was arranged in three stages, i.e. 18 discs oriented in each stage. Effect of major operating and physical variables such as hydraulic retention time (HRT), disc submergence and disc rotational speed were examined in COD removal. For duration of 5 days, 96.4% BOD removal was achieved in batch experiment. BOD constant rate (k) and ultimate BOD were determined respectively, 0.8198 day⁻¹ and 6349 mg/l by Thomas graphical method. COD removal efficiency was increased from 85.3 to 97.4% while the HRT was increased from 24 to 48 h. The COD removal efficiency increased from 74.9 to 87.5% as the disc submergence was increased from 31 to 36%. At submergence level of 23.7%, removal efficiency was increased due to activation of second and third compartments. When the rotational speed was increased from 3 to 11 rpm, the COD removal efficiency was also increased from 62.7 to 93.7%, respectively. The stage COD removal efficiency was gradually decreased with an increase number of stage and about 88% of organic compounds were removed in the first stage of aerobic RBC, indicating that the single stage reactor may be sufficient in practical application.     

Polishing domestic wastewater on a subsurface flow constructed wetland: organic matter removal and microbial monitoring

Microbial monitoring of constructed wetlands (CWs) treating domestic wastewater is generally scarce, despite the need of more knowledge about its biocenosis. The sanitation quality of a wastewater treated in a CW is a crucial aspect, mainly when the receiving water body is used as a swimming and/or recreation area. The present study was carried out in a horizontal subsurface flow CWplanted with Phragmites australis receiving pre-treated domestic wastewater (mean flow 50 m3 day(-1)), from a population of about 300 inhabitants. The monitoring programme undertaken during the first year operation, revealed removal efficiencies of 61% BOD5, 44% COD, and 65% TSS for inlet water with ca. 90 mg L(-1) BOD5, 157 mg L(-1) COD, and 17 mg L(-1) TSS. Total Coliform (TC) and Faecal Coliform (FC) bacteria were removed from wastewater (mean inlet values of 5 x 10(6) CFU 100 mL(-1) TC and of 9 x 10(5) CFU 100 mL(-1) FC), with efficiencies of 92 and 97%, respectively. The dynamics of microbial communities established in the system assessed by polymerase chain reaction-denaturing gradient gel electrophoresis (PCR-DGGE), had revealed a high bacterial diversity within the system, with no relevant differences in composition at the CW inlet and outlet but exhibiting temporal differences in bacterial communities.