人工湿地对猪场废水有机物处理效果的研究

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 4季测试 ,研究其对猪场废水有机物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 ,4个季节香根草或风车草人工湿地对COD和BOD有较稳定的去除效果 ,两湿地抗有机负荷冲击能力强 .在春季 ,停留时间 1～ 2d ,COD和BOD去除率分别为 70 %和 80 %;在夏季 ,进水COD高达 10 0 0～ 140 0mg·L-1情况下 ,COD去除率接近 90 %;在秋季 ,停留时间 1～ 2d ,COD和BOD去除率分别为 5 0 %～ 6 0 %和 5 0 %;在冬季 ,进水COD达 10 0 3mg·L-1情况下 ,COD去除率在 70 %以上 .COD、BOD和SS的去除率在两湿地间没有显著差异 .人工湿地污染物 (Y)随水力停留时间 (t)延长的降解遵从指数方程规律Yt=Y0 ·e( -kt) .在相同停留时间时 ,随进水污染物浓度 (x)提高的出水污染物浓度 (y)的回归关系遵从直线方程规律 y =a+bx .     

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.     

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17.0m²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P18.49 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.     

刈割对人工湿地风车草生长及污水净化效果的影响

刈割对人工湿地植物的生长和净化作用的影响,国内外学者的意见存在分歧。实验于2010年7月至2011年1月在华南师范大学生物园进行。利用水池(2m×2m×0.6m)构建风车草人工湿地生活污水处理系统,研究了刈割对人工湿地风车草生长和污水净化效果的影响。结果表明,刈割组风车草在整个实验过程中均保持着良好的生长态势,而对照组在11月以后生长减缓。刈割组风车草2010年7月至2011年1月的累积地上生物量、累积地上氮磷含量以及新增分蘖数均大于对照组,表现为超补偿生长。刈割组风车草的叶绿素含量、净光合速率、蒸腾速率和气孔传导率均显著高于对照组。刈割组和对照组的TN、TP、NH4-N和NO3-N的平均去除率分别为77%、84%、64%、72%和65%、67%、55%、63%,前者显著大于后者。刈割组和对照组的CODcr和BOD5平均去除率分别为58%、79%和54%、76%,两者差异不显著。总之,刈割对人工湿地风车草的生长和污水净化效果有明显的促进作用,这可为风车草人工湿地的科学管理提供参考。     

潜流-上行垂直流复合人工湿地对氮磷去除效果

研究了潜流-上行垂直流复合人工湿地工艺对NH4+-N、NO3--N、TN和TP的去除效果。在处理负荷为30 L.d-1,水力停留时间为4.8 d时,该工艺对NH4+-N、NO3--N、TN和TP具有良好的去除效果,平均去除率分别为95%、52%、79%和81%。对3种含氮化合物的去除效果可以根据运行时间分为两阶段,在两阶段中,对NH4+-N、NO3--N和TN的平均去除率分别为93%和99%,35%和98%,71%和98%。对TP的去除效果在整个试验过程中则保持稳定。     

浮床植物净化生活污水中N、P的效果及N2O的排放

在温室内采用浮床无土栽培技术,研究了黑麦草(Lolium mutliflorum)、水芹(Oenanthe javanica)和香根草(Vetiveria Zizanioides)3种植物对生活污水中N、P的去除效果及净化过程中N2O的排放特征。结果表明,浮床植物系统对生活污水的TN、NH4 -N和TP具有良好的净化效果。同对照系统相比,浮床黑麦草、水芹和香根草系统对TN的平均去除率分别提高了26.2%,22.9%,4.1%;对NH4 -N的去除率分别提高了31.4%,14.5%,3.0%;对TP去除率分别提高了33.1%,54.2%,15.5%。净化周期内,浮床各系统的TN、NH4 -N和TP浓度随着污水停留时间的延长直线下降,而NO3-N浓度却因系统内硝化强度大于反硝化强度而产生了累积;植物的存在明显的促进了浮床系统的N2O排放,浮床黑麦草、水芹、香根草和对照系统N2O的平均排放通量分别为174.44μg/(m2.h),82.19μg/(m2.h),112.49μg/(m2.h)和44.81μg/(m2.h)。浮床系统N2O排放通量的日变化呈现出夜间下降而白天增加的规律,与温度的昼夜变化规律基本相同,表明温度的升降直接影响了N2O的生成及排放。     

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。     

柊叶和象草波式潜流人工湿地的对比研究

为探索柊叶和象草在人工湿地中的应用及其净化机理,该研究以柊叶和象草为人工湿地植物分别构建了波式潜流人工湿地系统,分析了柊叶和象草波式潜流人工湿地对生活污水中COD_(cr)、TN和TP的净化效果,观察了柊叶和象草两种植物在不同季节的生长状况。结果表明:经过15个月的连续运行,在表面水力负荷约0.3 m·d~(-1)的条件下,柊叶和象草波式潜流人工湿地平均去除率是COD_(cr)分别为66.1%和70.1%,TN分别为60.4%和63.7%,TP分别为74.1%和75.1%。两种植物生长良好,根系发达,象草的地上生物量是柊叶的2.1倍,地下生物量相当;冬季象草生长缓慢,柊叶部分叶片的四周干枯,但二者都不会枯亡。这说明两个人工湿地对COD_(cr)、TN和TP都具有较好的去除效果,但无显著性差异,柊叶和象草能明显提高潜流人工湿地的净化效果。     

四种湿地植物在人工湿地的生长特性研究

研究了表面流人工湿地中香根草(Vetiveria zizanioides)、风车草(Cyperus flabelliformis)、芦苇(Phrogmites australis)和水鬼蕉(Hymenocallis littoralis)4种植物的根生物量和生长量、根系分布、地上部分的生长情况.风车草、香根草和水鬼蕉根系及地上部分的生长节律相似,9月或10月前生长较快,以后生长减慢甚至停止;芦苇则不同,7月以前生长缓慢,以后生长加速,冬季也保持较快的生长.全年根生长量和根生物量以水鬼蕉最大,显著高于其它植物(P<0.01),香根草最小,显著低于其它3种植物(P<0.01).香根草的根系垂直向下生长,分布较深,而其它3种植物的根系主要分布在浅层土壤中.风车草分株最多,叶面积指数最大.香根草叶面积指数最小.结果表明,在构建多种植物人工湿地群落时,可以考虑将芦苇与大多数湿地植物搭配以保证湿地全年保持较好的净化效果;水鬼蕉可以作为底层植物,和风车草等生长早、植株较高的植物构建多种湿地群落.     

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.     

Preparation of ultra-lightweight sludge ceramics (ULSC) and application for pharmaceutical advanced wastewater treatment in a biological aerobic filter (BAF)

Novel media-ultra-lightweight sludge ceramics (ULSC) employed in an upflow lab-scale biological aerobic filter (BAF) were investigated for pharmaceutical advanced wastewater treatment. The influences of the volume ratio of pharmaceutical wastewater to domestic wastewater (PW/DW), hydraulic retention time (HRT) and air-liquid ratio (A/L) on chemical oxygen demand (CODCr) and ammonium (NH(4)(+)-N) of the effluent were investigated. When PW/DW of 4:1, HRT of 6 h, and A/L of 5:1 were applied, the mean effluent concentration of NH(4)(+)-N was 6.2 mg L(-1), and the maximum CODCr concentration in the effluent was 96 mg L(-1). Both NH(4)(+)-N and CODCr did not exceed the limits of the national discharge standards (NH(4)(+)-N ≤ 15 mg L(-1), CODCr ≤ 100 mg L(-1)). In addition, the BAF system showed a strong capacity of further removal from NH(4)(+)-N of the effluent.     

膜-生物硝化反应器处理含氨废水效能的研究

研究了膜 生物硝化反应器对含氨废水的处理效能以及分离膜的截留和渗透效能。膜_生物反应器启动迅速 ,在水力停留时间为 1d的情况下 ,反应器最高进水浓度达 80mmol(NH₄⁺-N)·L^-1 ,最高容积负荷达 1 12kg(NH₄⁺ -N)·m^-3·d^-1 ,氨氮去除率保持在 95%以上。试验证明 ,分离膜对微生物有良好的截留作用 ,50天内反应器的污泥浓度从 5g·L^-1 增长到 10g·L^-1 ,分离膜表面附着的生物层则对废水氨氮和亚硝氮有进一步的转化作用。在液位差低于 80cm时 ,提高液位差可增大膜渗透通量 ;液位差超过 80cm后 ,增大液位差的膜渗透通量效应很小 ;其中 ,当液位差为 2 0cm左右时 ,膜通量达 2 . 5 1L·m^-2 ·h^-1 ,阻力最小 [(2 . 6 3× 10^-5)m^-1]。该膜_生物硝化反应器可依靠液位差压力驱动出水 ,无需外加动力。     

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。     

Effect of sludge-fly ash ceramic particles (SFCP) on synthetic wastewater treatment in an A/O combined biological aerated filter

Novel media-sludge-fly ash ceramic particles (SFCP) employed in an upflow lab-scale A/O BAF were investigated for synthetic wastewater treatment. The influences of hydraulic retention time (HRT), air-liquid ratio (A/L) and recirculation on the removals of chemical oxygen demand (CODcr), ammonia (NH(4)(+)-N) and total nitrogen (TN) were discussed. The optimum operation conditions were obtained as HRT of 2.0 h, A/L of 15:1 and 200% recirculation. Under the optimal conditions, 90% CODcr, more than 98% NH(3)-N and approximately 70% TN were removed. The average consumed volumetric loading rates for CODcr, NH(4)(+)-N and TN with 200% recirculation were 4.06, 0.36 and 0.29 kg(m(3)d)(-1), respectively. The CODcr and TN removal mainly occurred in the anoxic zone, while nitrification was completed at the height of 70 cm from the inlet of the bottom due to a suitable column layout of biological aerated filter (BAF). The characteristics of wastewater and backwashing affected TN removal to a large degree. In addition, the features of media (SFCP) and synthetic wastewater contributed to a strong buffer capacity in the BAF system so that the effluent pH at different media height fluctuated slightly and was insensitive to recirculation.     

Biological nitrogen removal using a vertically moving biofilm system

In this study, a biological nitrogen removal process using a vertically moving biofilm system was used to treat synthetic wastewater. The process consisted of two pre-denitrification units, one combined carbonaceous removal/nitrification unit and three nitrification units. Each unit employed biofilm growth on a plastic module. In the anoxic units, the modules were vertically moved, while always submerged, in the bulk fluid; in the aerobic units, they were moved vertically up into the air and down into the wastewater. Three small-scale experiments, having different recirculation ratios and influent loadings, were conducted at a controlled temperature of 11 degrees C. In this system, the carbonaceous removal efficiency was in the range of 94-96% and the total nitrogen removal efficiency was 77-82%. In the anoxic units, the denitrification efficiency was 94-98% and the areal denitrification rates, based on the surface area of the biofilm modules, were 2.9-3.8 g NO3-N/(m2 x d). The nitrification efficiency occurring in the aerobic tanks was up to 95% and the maximum areal ammonium removal rates were 1.3-1.8 g NH4-N/(m2 x d).     

Purification of nitrate-rich agricultural runoff by a hydroponic system

The purification of nitrate-rich agricultural runoff by a floating-raft (FR) hydroponic system was investigated at 3-, 2- and 1-d hydraulic retention times (HRTs) with particular emphasis on nitrogen conversion and removal through the system. The FR system has a dissolved oxygen (DO) environment similar to the horizontal subsurface flow system, generally 0.00mgL(-1), that facilitates denitrification. An efficient nitrate-nitrite-nitrogen (NO(x)-N) removal, 91%, 97% and 71% on average at 3-, 2- and 1-d HRT, respectively, was frequently achieved. The mean retentions were 17-47% for chemical oxygen demand, 31-64% for total nitrogen, and 8-15% for total phosphorus for the FR system. Mass balance analysis implied that the detectable DO concentration in the reactor, as low as 0.7mgL(-1), played a very important role in the conversion and removal of NH(3)-N and NO(x)-N, which finally affected the NO(x)-N removal at 3-d HRT.     

A novel microbial fuel cell and photobioreactor system for continuous domestic wastewater treatment and bioelectricity generation

A system containing a sequential anode-cathode configuration microbial fuel cell and a photobioreactor was developed for continuous treatment of wastewater and electricity generation. Wastewater was treated by the fuel cell to decrease the chemical oxygen demand (COD), phosphorus and nitrogen and to produce electricity. The effluent from the cathode compartment of the cell was continuously fed to an external photobioreactor to remove the remaining P and N using microalgae. Alone, the fuel cell generated a maximum power of 20.3 W/m(3) and achieved removal of 85 % COD, 58 % total phosphorus (TP) and 91 % NH(4) (+)-N. When coupled with the photobioreactor, the system removed 92 % TP and 99 % NH(4) (+)-N. These results demonstrate both the effectiveness and the potential application of the coupled system to continuously treat domestic wastewater and simultaneously generate electricity.     

Simultaneous sludge reduction and nutrient removal (SSRNR) with interaction between Tubificidae and microorganisms: a full-scale study

A symbiotic ecosystem between Tubificidae and microorganisms was established at a full-scale wastewater treatment plant (WWTP). In this ecosystem Tubificidae were inoculated, and then adhered to the outer layers of carrier materials in an oxidation tank. During the long-term treatment of sewage volumes of 20,000 m(3)d(-1), the excess sludge production rate was reduced from 0.21 to 0.051 kg m(-3) and sludge settleability was significantly improved. When the influent concentrations of COD, NH(4)(+)-N, PO(4)(-)-P, and SS were in the ranges of 130.0-459.0 mg L(-1), 14.2-27.5 mg L(-1), 1.6-7.0 mg L(-1), and 60.0-466.0 mg L(-1), respectively, the COD and SS removal efficiency was increased by 8.7% and 13.6% within the symbiotic system compared to the control without Tubificidae. In addition, NH(4)(+)-N and phosphorus removal efficiency can also be improved. The results showed that both sludge reduction and nutrient removal were enhanced simultaneously significantly within the system utilizing the symbiotic interactions of Tubificidae and microorganisms.