小球藻去除水产加工废水中氨态氮的初步研究

目的：确定小球藻去除水产行业加工废水中氨态氮的优化环境条件,为利用小球藻处理此类废水的规模化发展提供基础的实验数据。方法：在静止摇瓶培养方式下,逐一改变废水与小球藻培养液的混合体系的初始pH、温度或光照强度等条件,定时测定体系的氨态氮含量,并根据其随培养时间的变化确定优化环境条件。结果：当小球藻藻液的初始浓度为1×10~6个/mL左右,且小球藻培养液与水产加工废水的配比为3：2时,小球藻去除氨态氮的优化环境条件为：初始pH 7．5、培养温度25℃、光照时间12h/d,光强5300k,此时氨态氮的去除率达到77%。结论：实验条件下小球藻能够较好地去除水产加工废水中的氨态氮,为小球藻规模化处理此类废水提供了基础数据。     

pH值对沼液培养的普通小球藻生长及油含量积累的影响

以50％的沼液为普通小球藻的全营养培养基,考察培养基的起始pH值对小球藻生长及油脂含量的影响,普通小球藻对不同初始pH的沼液中氮、磷的去除情况。设定了2组实验,一组只调节初始接种培养液的pH,分别为6.0、6.5、7.0、7.5、8.0、8.5;另一组将培养液pH分别固定在6.0、6.5、7.0、7.5、8.0、8.5,pH用稀HCl和NaOH进行调节。研究发现在pH 6.5和pH 7.0的偏酸环境有利于小球藻生长,而pH在7.0~8.5的偏碱性条件下有利于小球藻油脂的积累,因此综合小球藻生长和油脂积累2个因素,得到最适合小球藻生长和油脂积累的pH为7.0。培养结束后沼液中氮磷的去除率分别达到了95％和97％,沼液中的总氮由原来的134.91 mg/L降至4.86 mg/L,总磷由10.19 mg/L降到0.32 mg/L。     

新型异养硝化-好氧反硝化菌Paracoccus sp. QD-19的分离及脱氮特性研究

从沈阳市南部污水处理厂活性污泥中分离获得同时具备异养硝化和好氧反硝化能力的新型菌株,研究其脱氮特性,为改善污水厂的脱氮处理工艺奠定基础。对菌株进行形态学观察和16S rRNA基因鉴定;分别以NH₄Cl、NaNO₂、KNO₃为唯一氮源探究菌株的脱氮能力;以碳源、C/N比、pH值、温度、转速、接种量(V∶V)等因素对菌株脱氮效果的影响进行研究。获得一株新型异养硝化-好氧反硝化菌株,经16S rRNA基因序列比对为副球菌属(Paracoccus),命名为Paracoccus sp. QD-19。菌株对初始氨氮浓度在300 mg/L以下的低浓度氨氮去除率能够达到100%,去除速率为8.707 mg/(L·h)且在脱氮过程中几乎没有亚硝态氮和硝态氮的积累。以亚硝态氮和硝态氮作为唯一氮源时,对此两种氮源的去除率36 h内均能达到99%,去除速率分别为4.944和5.666mg/(L·h)。确定了去除氨氮的最佳脱氮条件：琥珀酸钠为碳源,C/N比为10,pH值为7,接种量(V:V)为1%,温度为30℃,转速为140 r/min。菌株Pa...     

毛枝藻对人工污水脱氮除磷能力的研究

文章探究了2株毛枝藻(Stigeoclonium sp.)SHY-370及HB1617在不同初始氨氮浓度以及不同氮磷比条件下的生长情况与氮磷去除能力。结果表明氨氮浓度对2株毛枝藻的生长及TP去除能力均有一定的影响, SHY-370可耐受最大氨氮浓度为10 mg/L, HB1617为5 mg/L;氨氮浓度为1—10 mg/L时SHY-370及HB1617对其去除率均达到97%以上,最大去除速率为3.98 mg/(L·d)。氮磷比对SHY-370的生长影响不大,但在氮磷比大于20时HB1617的生长受到抑制; SHY-370对NO_3~--N去除的最佳氮磷比为10—40, HB1617为2—10;氮磷比为2时水体中TP的含量超过了SHY-370及HB1617所能去除的最大值,去除率较低。实验结果表明SHY-370及HB1617在污水深度脱氮除磷方面具有一定的潜力,可考虑将其应用于城市生活污水二级出水(TN≤15 mg/L、TP≤0.5 mg/L、 NH_4~+-N≤5 mg/L)的深度处理。     

氮磷浓度对藻-溞-草间相互作用的影响

为了解氮磷浓度对生物操纵效果的影响, 以小球藻、大型溞和金鱼藻分别作为浮游植物、浮游动物和大型沉水植物的代表, 建立了它们之间相互作用的水生微宇宙模型。研究了在25℃、2000—3000 lx 的温度和光照下, 不同氮磷浓度对三者生长的影响。结果表明: 两者共培养时, 在高氮(10.5 mg/L)条件下, 磷浓度小于0.1 mg/L 对大型溞繁殖和金鱼藻的生长有利; 磷浓度介于0.1—2 mg/L 时小球藻呈大暴发趋势, 而金鱼藻的生长则明显受抑制。在低氮(0.5 mg/L)条件下, 磷浓度不大于0.5 mg/L, 大型溞对小球藻有较好的抑制作用, 金鱼藻与小球藻无显著互抑现象; 磷浓度增大为2 mg/L 时, 小球藻对金鱼藻生长产生明显抑制。在0.05—2 mg/L 的磷浓度范围及高氮和低氮条件下三者共培养时, 大型溞数量及金鱼藻生物量均不同程度的升高,且小球藻数量得到了有效抑制, 以磷浓度为0.1—0.5 mg/L 时效果最佳; N/P 比值对藻、溞、草间的相互作用有重要影响, 在藻-溞系统中, 大型沉水植物的加入可以大大提高控藻效果, 减小N/P 比值波动带来的不利影响。与低氮情况相比, 高氮条件对金鱼藻、大型溞及小球藻的增长均存在一定抑制作用。磷浓度为0.5 mg/L时的水体氮磷去除效果好于其他磷浓度梯度。       

沼泽红假单胞菌去除镉的研究

研究了沼泽红假单胞菌(Rhodopseudomonas palustris)S菌株的生长、Cd2 的去除与供氧光照、碳源、pH及温度的关系。结果表明:在好氧黑暗、苹果酸为碳源、pH7.0和30℃条件下,S菌株对初始浓度为25mg/L的Cd2 去除率最大,达到85%。在最佳条件下,Cd2 初始浓度为10mg/L~25mg/L时,去除率达85%,Cd2 浓度增加到150mg/L时,去除率仅为23%。测定Cd2 在菌体不同部位的分布发现菌体中富集的Cd2 63.5%在细胞壁上,33.5%在细胞原生质体内。同时,结合该菌体细胞超薄切片透射电镜观察证明了S菌株对Cd2 的去除主要在细胞壁上。     

利用Chlorella vulgaris C9-JN2010去除蓝藻-猪粪沼液废水中氮磷的研究

利用普通小球藻Chlorella vugaris C9-JN2010处理蓝藻-猪粪沼液废水,以实现废水无害化利用。实验考察了氮磷比和沼液浓度对小球藻生长及处理废水效果的影响,结果表明:在氮磷比(20:1)和沼液浓度(5%)条件下培养小球藻,藻细胞生长和废水处理效果最佳,最高细胞干重及生产强度分别为900.1 mg·L~(-1)和85.1 mg·L~(-1)·d~(-1),废水中总氮、总磷、氨氮的去除率分别为84.6%、95.9%和90.5%,对应去除强度分别为5.43 mg·L~(-1)·d~(-1)、0.30 mg·L~(-1)·d~(-1)和4.75 mg·L~(-1)·d~(-1)。利用小球藻可较彻底的去除蓝藻-猪粪沼液废水中氮、磷等营养,达到污水处理效果。     

小球藻吸附水中Pb2+影响因素的初步研究

对小球藻生物吸附水中Pb2 + 的影响因素作了初步研究。实验表明 :在小球藻处于指数生长期和静止期时加入Pb2 + ,去除率达 6 0 %以上 ;当藻细胞密度一定时 ,随着Pb2 + 浓度的增加 ,Pb2 + 的去除率增大 ;当Pb2 + 浓度一定时 ,随着藻细胞密度的增加 ,小球藻对Pb2 + 的去除率增大 ,藻细胞密度为 1 2 9× 10 8个 /ml时 ,去除率可达 92 82 % ;加强光照可以促进小球藻对Pb2 + 的吸附 ;在pH值为 5～ 10的范围内 ,pH对Pb2 + 吸附影响不大 ,较佳的pH值在 7左右。实验最佳条件的去除率在 90 %以上 ,去除效果较好。     

水网藻(Hydrodictyon reticulatum)治理水体富营养化的可行性研究

研究了不同形态的氮及磷浓度对水网藻的生长及吸收去除氮磷能力的影响;并对水网藻在我国南方供水水库GDAR现场的生长能力作出评价。水网藻在氮磷比为15左右的条件下,生长及氮,磷去除能力均为最好,并能优先吸收氨氮。在总氮、总磷分别为4.5mg/L和0.3mg/L时,对总氮和总磷的3d去除率几乎达100％。水网藻在水库现场全年均能正常生长。夏、秋和冬3个季度的生长率分别为1.051、0.557和0.353。实验证明水网藻可以作为改善我国南方富营养化水库水质的一种辅助措施。     

小球藻净化污水中氮磷能力的研究

在小球藻液中分别添加不同浓度的N、P溶液,研究小球藻净化氮、磷的能力。实验结果表明,氮磷组合浓度不同时对小球藻吸收氮、磷有一定影响;在最佳pH为8.0-8.5的条件下,吸收率可达80％左右;升高温度或加强光照有利于小球藻对磷、氮的吸收。小球藻对氮、磷的吸附随着培养时间的延长而逐渐升高。     

粗甘油优化污泥脱水液培养小球藻过程的研究

污泥脱水液为污泥压缩过程产生的污水,因其含有N、P等营养物,可用于微藻的培养。但污泥脱水液碳氮比低,可利用碳源有限,影响微藻生长。本研究考察外加不同浓度(1 g/L,2 g/L,4 g/L,6 g/L)生物柴油副产物-粗甘油对污泥脱水液培养小球藻过程的影响。结果表明:1 g/L、2 g/L粗甘油浓度能促进小球藻生长,藻生物量为1.29 g/L、1.45 g/L;2 g/L粗甘油浓度下氨氮、总氮去除率达99.32%和97.52%。粗甘油被分解后易使培养体系pH降至7以下,使总磷去除率比对照组略低。外加1 g/L、2 g/L粗甘油组的COD去除量分别为553.00 mg/L和405.00 mg/L。藻细胞元素和傅里叶红外光谱分析表明补加粗甘油后藻细胞中C元素和H元素相对含量均明显增加,C元素含量约为对照组的1.5倍;2 g/L粗甘油组的蛋白质与脂类物质含量均高于对照组。MPBR半连续培养小球藻过程中,HRT为5 d时藻生物量维持在1.99~2.21 g/L,大约为批次生物量的1.50倍;氨氮、总氮、总磷、COD的去除率分别在96.26%~99.20%、92.44%~94.04%、53.63%~58.58%、59.44%~65.57%。     

乙酸驱动条件下粪产碱杆菌Y5的碳氮共脱除特性

【目的】研究微生物的碳氮共脱除特性及其关键影响因素。【方法】以乙酸为唯一碳源分离获得的碳氮共脱除菌株Y5为模式菌株,分析菌株Y5的16S r RNA基因序列、碳源和氮源去除动力学,以及碳源种类、碳氮比(C/N)、溶解氧浓度(DO)、温度和p H等影响效果。【结果】菌株Y5归属于粪产碱杆菌。与葡萄糖及多种有机酸相比,菌株Y5在以乙酸为唯一碳源的条件下具有较高的TOC和NH4+-N去除速率。在好氧条件下,当起始TOC浓度为1 000 mg/L,氨氮浓度为110 mg/L时,菌株Y5的NH4+-N、TOC和总氮(TN)去除率分别达99.54%、92.95%和86.55%,最大NH4+-N、TOC和TN去除速率分别为903.58、505.81和406.03 mg/(L·d)。【结论】粪产碱杆菌Y5在以乙酸为唯一碳源的条件下具有较强的碳氮共脱除能力,其最佳反应条件为:C/N=10,p H 7.0-8.0,溶氧6.20 mg/L,反应温度为30°C。     

基于好氧反硝化及反硝化聚磷菌强化的低温低碳氮比生活污水生物处理中试研究

【背景】低碳氮比生活污水很难达标处理,多级A/O工艺、生物强化技术及生物膜技术的有机结合可有效解决这一问题。【目的】开发出一种泥膜共生多级A/O工艺并进行中试研究,驯化出高效脱氮除磷菌剂并对系统进行生物强化。【方法】通过测定中试设备出水及污水处理厂出水化学需氧量(Chemical oxygen demand,COD)、氨氮(NH_4~+-N)、硝氮(NO_3~--N)、总氮(Total nitrogen,TN)、总磷(Total phosphorus,TP)对比分析两种工艺的污染物去除效能,利用高通量测序技术对比生物强化技术对系统微生物群落结构的影响。【结果】中试设备对COD、NH_4~+-N、NO_3~--N、TN、TP的去除效果均优于污水处理厂的处理工艺;驯化的低温好氧反硝化菌TN去除率最大值可达84.21%,驯化的低温反硝化聚磷菌群对磷的去除率最高可达85.75%;利用驯化菌群对中试设备进行生物强化后较好地改善了系统NH_4~+-N、NO_3~--N、TN、TP的去除效果;经生物强化后,具有好氧反硝化和反硝化聚磷功能的Pseudomonas菌群明显增多。【结论】泥膜共生多级A/O工艺对于低碳氮比生活污水的处理具有很好的效果,利用生物强化技术可有效提高低温条件下系统污染物去除效能。     

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.     

华南赤红壤无机复合肥氮磷淋失特征

采用室内土柱淋溶模拟试验,研究了不同施肥水平下无机复合肥中氮和磷在华南赤红壤中的淋失特征.结果表明: 铵态氮、硝态氮和总氮淋失量均随施肥量增加而提高;肥料中氮的淋失率在36.8%～49.2%之间,总氮淋失量（y）与施肥量（x）之间的回归方程为y=0.3667x+66.483（R²=0.992）;铵态氮和总氮的淋失主要集中在前5次淋洗,硝态氮的淋失持续时间更长.施肥量对可溶性磷淋失量无显著影响,但颗粒磷和总磷淋失量均随施肥量增加呈上升趋势;肥料磷淋失率在0.002%～0.010%之间,总磷淋失量（y）与施肥量（x）之间的回归方程为y=7e^-5x+0.0538（R²=0.931）;磷的淋失动态与氮显著不同,为缓慢的持续累积过程.硝态氮与铵态氮淋失量比值和可溶性磷与颗粒磷淋失量比值均随施肥量增加呈下降趋势.     

金属离子对粪产碱杆菌C16的脱氮和亚硝酸盐积累的影响

【目的】研究不同金属离子对异养氨氧化细菌C16的生长和脱氮性能影响,探讨适于C16生长和脱氮的金属离子及其浓度。【方法】实验选用Mg2+、Mn2+、Fe2+、Cu2+、Zn2+5种金属离子,对C16的生长﹑脱氮性能﹑亚硝酸盐氮积累以及相关酶活性进行研究。【结果】Mg2+明显促进C16的生长和NH4+-N氧化速率;较高浓度Mn2+使得C16无法生长;原培养基中缺少Fe2+会抑制C16的生长和NH4+-N氧化速率;在原培养基中加入0.1 mmol/L的Cu2+对C16的生长和脱氮具有一定的促进作用,Cu2+使得培养基中基本无NO2--N和NH2OH的积累;不同浓度的Zn2+对C16的生长和氨氮去除有抑制作用。酶活实验结果显示,0.1 mmol/L Mg2+促进了羟胺氧化还原酶(HAO)的活性;0.1 mmol/L Cu2+促进了硝酸盐还原酶(Nar)和亚硝酸盐还原酶(Nir)的活性。【结论】Mg2+是C16生长和脱氮过程中的一种重要金属离子;加入Cu2+可避免过量亚硝酸盐积累。     

Effect of L-glutamic acid on the growth and ammonium removal from ammonium solution and natural wastewater by Chlorella vulgaris NTM06

The main objective of this laboratory scale experiment was to study the effect of l-glutamic acid on the growth in media and removal of ammonium from ammonium solution and natural wastewater by Chlorella vulgaris NTM06. It was observed that higher levels (1.0% and 1.5%) of l-glutamic acid compared to control (0% l-glutamic acid) negatively affected growth of C. vulgaris NTM06 and enhanced removal of ammonium from ammonium solution as well as natural wastewater. After 24h of incubation, 99% of 169.3mg NH(4)(+)-N/l was removed from ammonium solution by 1.5% l-glutamic acid treated C. vulgairs NTM06 cultures; removal in case of control was 70%. In case of natural wastewaters with initial ammonium concentrations of 1550, 775, 310 and 155 mg NH(4)(+)-N/l, removal after 48 h of incubation were 60%, 88%, 61% and 55% respectively. Ammonium removals from ammonium solutions of pH 4.0-8.0 were similar, whereas adsorption of ammonium ions on to the surface of dead C. vulgaris NTM06 cells was around 11%. Compared to dark, cultures incubated under the light showed higher initial removal of ammonium, however, after 24h, differences were not significant. Further research on the role of l-glutamic acid in micro-algal treatment of wastewater and its combination with other approaches such as co-immobilization of micro-algae with other organisms, starvation of micro-algal cells and the use of polymers is recommended.     

Ammonia-nitrogen and orthophosphate removal by immobilized Scenedesmus sp. isolated from municipal wastewater for potential use in tertiary treatment

Scendesmus sp. isolated from municipal wastewater, entrapped in calcium alginate as algal sheets was employed to remove inorganic nutrients (N and P) from artificial and real domestic secondary effluents in parallel-plate bioreactor after starvation. The key factors affecting the removal efficiency (NH4+-N and PO4(3-)-P), system stability and reuse efficiency of screens were studied and discussed. It has been shown that cell density in the mixture of algal gel was the key factor compared with the thickness of the gel and the cell density of the reactor. A complete removal of NH4+-N and PO4(3-)-P was achieved within 4h of treatment in parallel bioreactors with the optimal cell density in the mixture of algal (2 x 10(8) algae mL(-1)) and 3mm gel sheets after second cycle. Nine cycles of wastewater treatment in 21 days were accomplished, holding higher removal efficiency. NH(4)(+)-N removal efficiency was 99.1% after 105 min, 100% after 135 min, PO4(3-)-P removal efficiency was 100% after 15 min in domestic secondary effluents. Immobilized Scendesmus sp. is shown to have great potentialities for removal of inorganic nitrogen and phosphorus from treated effluents.     

Potential of constructed wetlands in treating the eutrophic water: evidence from Taihu Lake of China

Three parallel units of pilot-scale constructed wetlands (CWs), i.e., vertical subsurface flow (VSF), horizontal subsurface flow (HSF) and free water surface flow (FWS) wetland were experimented to assess their capabilities in purifying eutrophic water of Taihu Lake, China. Lake water was continuously pumped into the CWs at a hydraulic loading rate of 0.64 m d(-1) for each treatment. One year's performance displayed that average removal rates of chemical oxygen demand (COD), ammonia nitrogen (NH(4)(+)-N), nitrate nitrogen (NO(3)(-)-N), total nitrogen (TN) and total phosphorous (TP) were 17-40%, 23-46%, 34-65%, 20-52% and 35-66%, respectively. The VSF and HSF showed statistically similar high potential for nutrients removal except NH(4)(+)-N, with the former being 14% higher than that of the latter. However, the FWS wetland showed the least effect compared to the VSF and HSF at the high hydraulic loading rate. Mean effluent TP concentrations in VSF (0.056 mg L(-1)) and HSF (0.052 mg L(-1)) nearly reached Grade III (0.05 mg L(-1) for lakes and reserviors) water quality standard of China. Wetland plants (Typha angustifolia) grew well in the three CWs. We noted that plant uptake and storage were both important factors responsible for nitrogen and phosphorous removal in the three CWs. However, harvesting of the above ground biomass contributed 20% N and 57% P of the total N and P removed in FWS wetland, whereas it accounted for only 5% and 7% N, and 14% and 17% P of the total N and P removed in VSF and HSF CWs, respectively. Our findings suggest that the constructed wetlands could well treat the eutrophic lake waters in Taihu. If land limiting is considered, VSF and HSF are more appropriate than FWS under higher hydraulic loading rate.