细菌和真菌对复合污染模拟废水的处理研究

本文利用胶质芽孢杆菌(Bacillus mucilaginosus)和黑曲霉(Aspergillus niger)处理铜-苯酚(简称铜-酚)和镉-苯酚(简称镉-酚)这类有机-无机复合污染模拟废水,采用胶质芽孢杆菌和黑曲霉分别单独、联合或先后处理等5种方式,探讨了这两类菌体对复合污染模拟废水的处理效果及优化方法。结果表明,微生物对铜-酚废水的处理效果优于对镉-酚废水。对于铜-酚废水的处理表明,当废水中苯酚浓度为50~200 mg/L时,去除率可达80%以上,最高可达94.65%,其中铜的去除率较苯酚低;当模拟废水中铜浓度为30 mg/L时,可达最高去除率(60.02%)。微生物对镉-酚废水的处理表明,当废水中镉离子浓度为4 mg/L时,最高去除率为58.44%,苯酚的去除率一直保持在30%左右。     

坡缕石粘土固定辣根过氧化酶处理硝基酚废水

以坡缕石粘土、淀粉、水玻璃为原料,研究了固定化酶载体的制备工艺,探究了固定化酶载体在辣根过氧化酶(HRP)降解硝基酚废水中的作用,并探讨了反应时间、酶浓度、H2O2及硝基酚浓度对降解效果的影响。结果表明,固定化酶载体的最佳制备工艺为:水玻璃12%,淀粉20%,煅烧温度550℃,煅烧时间2 h;固定化酶对硝基酚的去除效果明显高于原酶;固定化酶去除水中硝基酚的最佳反应条件为:反应时间1.5 h,加酶量150 U,H2O2浓度0.12%,硝基酚浓度100 mg/L;固定化酶重复使用7次后对硝基酚的去除率仍高于60%。     

MnO2-UV联用光化学降解苯酚废水的初步研究

探讨了人工合成的高价锰氧化物与紫外光(UV)联用时降解苯酚废水的特性。结果表明,氧化锰矿物在无UV时对苯酚的降解能力差异大,1 g/L的氧化锰4 h对200 mg/L苯酚废水的降解率和COD去除率分别为:锰钾矿97.51%、酸性水钠锰矿89.07%、碱性水钠锰矿11.36%、钙锰矿9.67%;锰钾矿87.79%、酸性水钠锰矿53.11%、碱性水钠锰矿6.42%、钙锰矿1.43%。UV光照下,氧化锰矿物对苯酚的降解率有不同程度的提高,且表现出显著的表面光催化性质,增加了苯酚的深度降解,COD去除率显著提高。UV下氧化锰4 h对苯酚的降解率分别为:锰钾矿99.48%、酸性水钠锰矿91.86%、碱性水钠锰矿40.15%、钙锰矿35.95%);COD的去除率分别为:锰钾矿98.11%、酸性水钠锰矿68.45%、钙锰矿27.57%、碱性水钠锰矿24.27%。MnO2-UV联用时降解苯酚可能包括两种主要作用机制:氧化锰矿物的直接化学氧化降解和UV下MnO2的表面光催化降解。     

锰钾矿光催化降解苯酚及其影响因素研究

利用回流法合成隧道结构的锰钾矿,并研究其光化学降解苯酚的效果及影响因素。分别采用X射线衍射、原子吸收光谱、扫描电镜、透射电镜和BET氮气吸附法对锰钾矿的晶体结构(包括晶型、晶胞参数和结晶度)、化学组成、微观形貌和比表面积进行了表征。研究表明,非光照时锰钾矿对苯酚的降解效果较差,光照能显著促进锰钾矿对苯酚的降解;光照条件下,p H值减小能显著促进锰钾矿对苯酚的降解;锰钾矿用量增加至1.00 g/L时能显著促进锰钾矿降解苯酚,但继续增加矿物用量却显著降低苯酚降解率;非光照条件下,p H值减小和矿物用量增加不能显著促进锰钾矿降解苯酚。     

固体酸SO42-/TiO2-SnO2-ZnO光催化降解苯酚废水

采用共沉淀-湿法研磨-焙烧法制备 SO42-/TiO2-SnO2-ZnO(简写 STSZ)型固体酸催化剂,通过X射线衍射光谱、吡啶-红外光谱和扫描电镜对固体酸催化剂进行表征;以紫外灯为光源,研究催化剂用量、反应温度、反应时间以及催化剂回收利用等因素对苯酚降解的影响。结果表明在苯酚浓度为20 mg/L时,催化剂加入量6 g/L,20 W 紫外灯光距10 cm,废水温度40℃下搅拌反应3 h后,苯酚降解率可达到79.3%;催化剂重复使用6次后效果降低约10.6%,催化剂再生后活性与新鲜催化剂相当。     

电气石粉对油田采出废水处理效果实验研究

将电气石粉应用于油田采出废水CODCr的处理中,实验表明处理效果主要受反应时间、电气石用量、电气石粒径和溶液pH值等因素的影响。通过正交实验得到处理的最佳条件为:溶液pH=9,反应时间60min,电气石用量200g/L,电气石粒径100μm,此时油田采出废水CODCr降至68.46mg/L,去除率达到了82.25%。结合紫外线、红外线、超声波等条件进行电气石粉的CODCr降解实验,结果表明,这3种方法是有效的,其中结合超声波处理使去除率达到了90%以上,结合紫外线使处理时间降低了83%。本实验的进行为电气石这种环境矿物材料拓宽了应用领域。     

Fenton氧化膜-生物反应器出水中丙烯腈的实验研究

采用膜-生物反应器和Fenton氧化组合工艺对丙烯腈废水进行处理。从GC/MS测量结果来看,膜-生物反应器出水中主要物质为2,6双（二甲基-乙基）-4-酚、苯二甲酸和硝基苯二甲酸,均为生物难降解有机物,使出水不能达标。后续Fenton氧化工艺处理膜生物反应器出水,可以使COD含量等指标达到所要求的排放标准。经过膜-生物处理与Fenton法结合的优化工艺,COD去除率达到80%~88%,去除率达到98%,出水水质可达排放标准。Fenton氧化工艺的最佳工艺条件为：pH值为3.4,硫酸亚铁的投加量为700mg/L,双氧水的投加量为600mg/L。     

Degradation of phenol of high concentration by FeAIOx/MMT catalyzed Fenton reaction

以蒙脱土为载体制备负载型Fe/Al复合氧化物（FeAlOx/MMT）用于催化Fenton反应降解高浓度苯酚废水。实验结果表明,活性相FeAlOx中Fe/Al摩尔比为0.22时制备所得催化剂对Fenton反应具有最佳活性,且Fe/Al复合氧化物并未嵌入蒙脱土层间。在低温和高pH条件下催化体系存在诱导期,诱导期内FeAlOx/MMT缓释出Fe离子并进而由Fe离子催化溶液中的Fenton反应。通过对非均相催化降解苯酚废水的动力学研究发现,H2O2初始浓度、溶液的pH和反应温度对COD降解效率具有显著影响。调节降解过程中的温度序列和氧化剂引入程序能够缓解高温和高双氧水浓度双重因素耦合导致的HO.自消耗。在优化的降解条件下使用理论用量的H2O2可使得1 g/L的苯酚废水中苯酚降解率达到100%,而COD的降解率则达到97%。     

地下水中三氯乙烯-苯酚的好氧共代谢的实验研究

以苯酚作为三氯乙烯（TCE）降解的共代谢基质,用瓦勃氏微量呼吸测压仪（简称瓦呼仪）作为测试手段,分析了经苯酚驯化后的混合微生物对苯酚、TCE的降解特性;并讨论了以苯酚作为共代谢基质时TCE降解的可能性。实验结果表明：未驯化的活性污泥不能降解TCE; 经苯酚驯化后的活性污泥,当TCE的质量浓度为50 μg/L时其降解效果较好,TCE的氧化率达3369%;TCE的质量浓度为100 μg/L时其降解效果较差,其氧化率仅为3.2%;苯酚和TCE共代谢降解时,苯酚的存在促进了TCE的降解,当苯酚质量浓度为40 mg/L、TCE质量浓度为50 μg/L时共代谢降解效果最好,TCE的氧化率为79.11%。     

紫外光及日光下天然金红石光催化降解苯酚的研究

研究了山西代县天然金红石在紫外光和日光照射条件下对苯酚的光催化降解性能,考察了光照时间、pH值、苯酚初始浓度以及H2O2添加量对降解过程的影响。在紫外光照射下,酸性条件(pH=3.5)利于光催化降解,中性和碱性条件下降解效率较低;当初始浓度为60mg/L时,降解速率可达1.922mg/(L.h);H2O2作为电子捕获剂可提高苯酚降解速率,最佳投加量为2mL/L。在日光条件下,天然金红石对苯酚表现出良好的降解性能,照射7h后,降解率达87.68%,仅略低于P25型TiO2(99.72%),可在14h内完全降解。根据电子探针和X射线衍射分析结果,认为天然金红石晶格中的V、Fe等杂质可能是提高其可见光响应效果和光催化活性的主要原因。     

Removal of phenolic compounds in olive mill wastewater by silica–alginate–fungi biocomposites

This study aims to attempt a treatment strategy based on fungi immobilized on silica-alginate (biocomposites) for removal of phenolic compounds in olive oil mill wastewater (OMW), OMW supplemented (OMWS) with phenolic compounds and water supplemented (WS) with phenolic compounds, thus decreasing its potential impact in the receiving waters. Active (alive) or inactive (death by sterilization) Pleurotus sajor caju was encapsulated in alginate beads. Five beads containing active and inactive fungus were placed in a mold and filled with silica hydrogel (biocomposites). The biocomposites were added to batch reactors containing the OMW, OMWS and WS. The treatment of OMW, OMWS and WS by active and inactive biocomposites was performed throughout 28 days at 25 °C. The efficiency of treatment was evaluated by measuring the removal of targeted organic compounds, chemical oxygen demand (COD) and relative absorbance ratio along the time. Active P. sajor caju biocomposites were able to remove 64.6–88.4 % of phenolic compounds from OMW and OMWS and 91.8–97.5 % in water. Furthermore, in the case of OMW there was also a removal of 30.0–38.1 % of fatty acids, 68.7 % of the sterol and 35 % of COD. The silica–alginate–fungi biocomposites showed a high removal of phenolic compounds from OMW and water. Furthermore, in the application of biocomposites to the treatment of OMW it was observed also a decrease on the concentration of fatty acids and sterols as well as a reduction on the COD.     

Enhanced bioremoval of refractory compounds from dyeing wastewater using optimized sequential anaerobic/aerobic process

The upflow anaerobic sludge blanket process followed by the biological aerated filter process was employed to improve the removal of color and recalcitrant compounds from real dyeing wastewater. The highest removal efficiency for color was observed in the anaerobic process, at 8-h hydraulic retention time, seeded with the sludge granule. In the subsequent aerobic process packed with the microbe-immobilized polyethylene glycol media, the removal efficiency for chemical oxygen demand increased significantly to 75 %, regardless of the empty bed contact time. The average influent non-biodegradable soluble chemical oxygen demand was 517 mg/L, and the average concentration in effluent from the anaerobic reactor was 363 mg/L, suggesting the removal of some recalcitrant matters together with the degradable ones. The average non-biodegradable soluble chemical oxygen demand in effluent from the aerobic reactor was 87, 93, and 118 mg/L, with the removal efficiency of 76, 74, and 67 %, at 24-, 12-, and 8-h empty bed contact time, respectively. The combined anaerobic sludge blanket and aerobic cell-entrapped process was effective to remove the refractory compounds from real dyeing wastewater as well as in reducing organic loading to meet the effluent discharge limits. This integrated process is considered an effective and economical treatment technology for dyeing wastewater.     

Color removal from industrial wastewater with a novel coagulant flocculant formulation

Chemically enhanced wastewater treatment is attracting substantial interest among the currently employed chemical unit processes in wastewater treatment. Coagulation-flocculation has received considerable attention for yielding high pollutant removal, especially color removal. This investigation presents a novel formulation of coagulation-flocculation for color removal from industrial wastewater and illustrates its efficiency, with aid of measurement of solid sludge content, suspended solid content, percentage of solid recovery, UV absorption in wastewater effluent from two automotive factories. The results show that the novel formulation can remove color content from wastewater efficiently. The treated wastewater had UV absorption close to distillated water and color was removed up to 96% by flocculation / coagulation treatment.     

表面流人工湿地处理糠醛生产废水的应用

根据糠醛生产废水的特点,利用生产企业所处低洼盐碱地改造成表面流人工湿地,废水在湿地内以自然消耗的方式处理,无外排,处理的废水量等于湿地内废水的自然蒸发量、植物的蒸腾量与植物的贮存量。研究表明,经湿地处理后的废水COD去除率平均为94%,TN去除率平均为65%,TOC去除率平均为94.9%。处理后的废水pH值为6.22。     

化学氧化技术异位处理地下水非水相有机污染物中试研究

选取某农药厂旧厂区为试验场地,考察化学氧化技术异位处理地下水非水相有机污染物的运行效果。基于小试研究,确定高锰酸钾、高铁酸钾、芬顿试剂以及次氯酸钠4种氧化剂在中试试验中的适宜投加量。中试结果表明,当进水流量为1.0 m^3/h时,不同氧化剂对于常规水质指标及特征有机污染物的去除效果存在差异性。总体而言,四种氧化剂对于中长链石油烃类污染物(C10-C36)的去除率可达20%~70%,但对氯代烷烃类污染物的去除效果低于20%;高铁酸钾和次氯酸钠分别对于苯酚类和多环芳烃类污染物的去除效果较好(70%~100%);芬顿试剂对各类污染物均有显著氧化效果,其中对于短链石油烃(C6-C9,去除率20%~40%)、苯系物(去除率40%~90%)的去除效果高于其他三种氧化剂。研究不同氧化剂对于多组分有机污染地下水的处理效果,为将化学氧化技术应用于此类污染场地提供了理论和技术支持。     

Potentials of phototrophic bacteria in treating pharmaceutical wastewater

A suspended growth photobioreactor was utilized to treat pharmaceutical wastewater by a wild strain purple non-sulfur photosynthetic bacterium isolated from the soil. The strain was named Z08 and identified as Rhodobacter-sphaeroides by 16SrDN. The photobioreactor was illuminated externally with two (40 W) fluorescent compact light sources on both sides. Its operation pH and temperature were between 6.8–7.0 and 20–30 °C, respectively. Optimum growth of the isolate was obtained after enrichment of the pharmaceutical wastewater with 0.5 % ammonium sulfate and 0.1 % yeast extract under microaerobic optimum light (6000 lx) condition at 5d retention. Using these optimum conditions, the maximum dry cell weight and chemical oxygen demand percentage removal were 880 mg/L and 80 %. Chemical analysis of the culture after treatment of the enriched and non-enriched wastewater showed the crude protein content of the biomass to be 54.6 % and 38.0 %, respectively. This study proved that photosynthetic bacteria could transform complex wastewater that contains recalcitrant organic compounds with a resultant recovery of useful products.     

人工快速渗滤复合系统处理洗浴污水的试验研究

针对传统污水快速渗滤土地处理系统水力负荷低，占地面积大的弱点，提出了采用人工砂和天然砂作为渗滤介质建立复合系统的试验方案，并以洗浴污水为研究对象进行了5个月的室内试验研究。结果表明，复合系统具有较高的水力负荷和较好的去污效果，其COD，BOD5，SS和阴离子洗涤剂（以MBAS代表）的平均去除率分别为86.25%,86.75%,98.95%和90.86%。处理出水中COD，BOD5，SS和阴离子洗涤剂的平均浓度分别为17.30,5.84,0.3和0.18mg/l。     

Moving bed biofilm reactor to treat wastewater

This review carries out a comparative study of advanced technologies to design, upgrade and rehabilitate wastewater treatment plants. The study analyzed the relevant researches in the last years about the moving bed biofilm reactor process with only attached biomass and with hybrid biomass, which combined attached and suspended growth; both could be coupled with a secondary settling tank or microfiltration/ultrafiltration membrane as a separation system. The physical process of membrane separation improved the organic matter and NH₄ ⁺-N removal efficiencies compared with the settling tank. In particular, the pure moving bed biofilm reactor–membrane bioreactor showed average chemical oxygen demand, biochemical oxygen demand on the fifth day and total nitrogen removal efficiencies of 88.32, 90.84 and 60.17%, respectively, and the hybrid moving bed biofilm reactor–membrane bioreactor had mean chemical oxygen demand, biochemical oxygen demand on the fifth day and total nitrogen reduction percentages of 91.18, 97.34 and 68.71%, respectively. Moreover, the hybrid moving bed biofilm reactor–membrane bioreactor showed the best efficiency regarding organic matter removal for low hydraulic retention times, so this system would enable the rehabilitation of activated sludge plants and membrane bioreactors that did not comply with legislation regarding organic matter removal. As the pure moving bed biofilm reactor–membrane bioreactor performed better than the hybrid moving bed biofilm reactor–membrane bioreactor concerning the total nitrogen removal under low hydraulic retention times, this system could be used to adapt wastewater treatment plants whose effluent was flowed into sensitive zones where total nitrogen concentration was restricted. This technology has been reliably used to upgrade overloaded existing conventional activated sludge plants, to treat wastewater coming from textile, petrochemical, pharmaceutical, paper mill or hospital effluents, to treat wastewater containing recalcitrant compounds efficiently, and to treat wastewater with high salinity and/or low and high temperatures.     

Statistical analysis of main and interaction effects during the removal of BTEX mixtures in batch conditions, using wastewater treatment plant sludge microbes

Biodegradation has proved to be a versatile technique to remediate benzene, toluene, ethyl benzene and xylene mixtures in contaminated soil and groundwater. In this study, a mixed microbial culture obtained from a wastewater treatment plant was used to degrade liquid phase ethyl benzene and xylene, at initial concentrations varying between 15 to 75 mg/l. Experiments were conducted according to the 2^k?1 fractional factorial design to identify the main and interaction effects of parameters and their influence on biodegradation of individual ethyl benzene and xylene compounds in mixtures. The removal efficiencies of these compounds varied between 2 to 90% depending on the concentration of other compounds and also on their interaction effects. A statistical interpretation of the results was done based on the Fishers variance ratio (F) and probability (P) values. Though all the main effects were found significant (P < 0.05) at the 5% confidence level, the interactions between benzene and toluene and benzene and xylene concentrations were also found to be statistically significant and play a major role in affecting the total ethyl benzene and xylene removal.