MFC-MBR耦合系统运行效果及产电性能

为了解决膜生物反应器(MBR)运行成本高、膜污染的问题,本研究建立了一个微生物燃料电池(MFC)-MBR耦合系统,通过MFC回收污水中的能量,同时控制膜污染。研究结果表明,耦合系统对COD和NH3-N的去除率分别为(94.6±3.0)%和(90.9±6.9)%,出水水质稳定。由于MFC的耦合作用,使MBR的运行周期由18 d延长至36 d,膜污染得到了明显的减缓。耦合系统中MFC产电性能稳定,电流密度稳定在5.7 A/m3,最大功率密度达到了928.0 mW/m3,循环伏安法(CV)表明,阴极附着的微生物具有良好的电化学催化作用。MFC-MBR耦合系统将污水中的化学能转化为电能从而实现了膜污染的减缓及能量的回收,显示出巨大的发展前景。     

一株光合细菌的分离鉴定及其产电特性

采用光照富集及厌氧划线法从污水厂二沉池活性污泥分离到一株光合细菌YC-1,结合菌落特征、细胞形态、活细胞吸收光谱及16S rRNA基因序列分析等对其进行了分类学鉴定,并研究了YC-1在不同光源照射下的产电性能。结果表明,该菌为短杆状,有鞭毛,菌落呈淡粉色,含有大量细菌叶绿素a,16S rRNA基因序列与Rhodopseudomonas palustris DX-1相似度为99%,属于假单胞菌属(Pseudomonas sp.);双室微生物燃料电池的阳极室接种YC-1,并以乙酸钠为底物,铁氰化钾作为阴极电子受体,外载为1 000Ω时,电池稳定运行时输出电压为0.58 V,且输出电压不受光源光谱影响。     

锰铜铈氧化物催化剂氧化NO性能及动力学研究

实验以TiO2为载体采用浸渍法制备CuOx/TiO2、CeOx/TiO2、CuCeOx/TiO2和MnCuCeOx/TiO2催化剂,考察这些催化剂氧化NO活性,探究Cu、Ce摩尔比和添加Mn元素对CuCeOx/TiO2催化剂氧化NO活性的影响,使用扫描电镜观察催化剂表面结构。研究发现,Cu、Ce元素配合后的CuCeOx/TiO2催化剂氧化活性明显好于单独含Cu、Ce的催化剂,当Cu、Ce摩尔比为Cu:Ce=1∶2时,CuCeOx/TiO2催化剂氧化活性最好,在NO浓度500×10-6,O210%,空速为24 000 h-1,350℃时,NO氧化度为0.62;添加Mn元素可以提高CuCeOx/TiO2催化剂低温氧化活性,250℃时,MnCuCe/Ti-3和MnCuCe/Ti-5催化剂氧化度为0.53和0.69,300℃时,MnCuCe/Ti-3和MnCuCe/Ti-5催化剂氧化度均为0.76;此外,实验还研究了NO在MnCuCe/Ti-3催化剂上反应的动力学方程。     

丝状菌污泥膨胀及其致密过程中菌丝体演替规律

为了探索丝状菌的致密途径、解决丝状菌污泥膨胀的难题,从丝状菌的自身特点及外部条件出发研究了其在污泥膨胀及致密过程中菌丝体的演替规律。研究发现,致密生长的大絮体对丝状菌的种类是有选择性的,那些丝体较弯曲、丝体强度较大、贮存能力强的菌丝体更利于形成聚集态生长。另外,研究表明,不同种类丝状菌的生长势和存贮能力不同,对底物的利用上亦存在着竞争关系。实验中存在的几个菌种对PHB颗粒的存贮能力由高到低依次为:Nostocoida limicolaⅡ、Type 1851、Type 0701、Type 021N型菌体。     

CdIn2S4/复合材料的制备及光降解罗丹明B

利用高压静电纺丝技术,制得含有羧基的导电聚合物纤维(聚偏氟乙烯/苯乙烯-马来酸酐共聚物/纳米石墨),高温水热条件下在纤维表面制备CdIn2S4颗粒,得到CdIn2S4/导电聚合物纤维复合材料。运用扫描电子显微镜(SEM)、X射线衍射仪(XRD)、紫外-可见吸收光谱仪(UV-Vis)和热失重分析仪(TGA)对复合材料的结构进行表征。并利用350 W氙灯模拟太阳光进行光催化降解罗丹明B。结果发现,CdIn2S4/导电聚合物纤维复合材料的降解效率高于CdIn2S4粉体和Degussa P25 TiO2粉体,光催化降解3 h,罗丹明B的降解率为96.2%。     

基于MODIS数据的安徽区域日蒸散量估算与分析

蒸散的估算在区域能量平衡和水资源研究中具有重要意义,遥感技术发展促进了区域蒸散的研究。利用安徽省气象资料、MODIS数据产品及GIS背景信息,基于SEBAL模型,按1 km空间分辨率进行了面尺度的安徽省日蒸散量估算,并在GIS空间分析模块的支持下对不同土地覆盖类型的日蒸散量进行统计分析。结果表明：遥感估算的蒸散量与利用Penman Monteith公式计算的蒸散量比较,两者之间具有较好的相关性,遥感蒸散估算值整体偏小,不同土地利用类型的日蒸散量间差异显著。遥感蒸散估算方法在安徽省具有一定的实用性,需优化模型参数,以提高其进一步技术推广的前景     

臭氧联用技术深度处理腈纶废水的效果对比

将臭氧分别与超声波、H2O2、紫外光等联用,深度处理干法腈纶生产厂生化池出水,对各种联用技术的处理效果进行了研究。实验结果表明：在进水流量2 L/min、反应时间30 min、臭氧加入量3.5 g/（L?h）的条件下,当超声功率为300 W时,臭氧-超声联用技术的COD去除率为30.0%;当H2O2加入量为0.4 mL/L时,臭氧-H2O2联用技术的COD去除率为50.7%;当紫外灯功率为40 W时,臭氧-紫外光联用技术的COD去除率为49.9%;在各种联用技术中,臭氧-H2O2联用技术的运行成本最低（为7.5 元/t）,且处理后出水COD为143 mg/L,达到《<污水综合排放标准>（GB8978—1996）中石化工业COD标准值修改单》中的一级排放标准。综合考虑,臭氧-H2O2联用技术是深度处理干法腈纶废水的最优工艺。     

Mn/γ-Al2O3催化剂的制备及头孢合成废水的催化臭氧氧化法深度处理

对Mn/γ-Al₂O₃催化剂的制备条件及头孢合成废水的催化臭氧氧化法深度处理工艺条件进行了优化。实验结果表明：以Mn（NO₃）₂溶液为浸渍液,Mn/γ-Al₂O₃催化剂的最优制备条件为浸渍液浓度0.10 mol/L、浸渍时间9 h、焙烧温度400 ℃、焙烧时间2 h;在反应时间为30 min、废水pH为9.0、臭氧通量为4.6 mg/min、催化剂加入量为5 g/L的条件下,当进水COD、BOD₅、ρ（氨氮）和色度分别为220~250 mg/L,8~10 mg/L,10~12 mg/L和60~70倍时,出水COD、BOD₅、ρ（氨氮）和色度的平均去除率分别为53%,30%,33%和93%,出水水质满足GB 21904—2008《化学合成类制药工业水污染物排放标准》的要求。     

Catalytic hydrolysis of urea from wastewater using different aluminas by a fixed bed reactor

In order to find an effective method for treating urea wastewater, the experiments on the hydrolysis of urea in wastewater were conducted in a fixed bed reactor with different aluminas (α-Al₂O₃, γ-Al₂O₃, and η-Al₂O₃) as catalysts respectively in contrast with inert ceramic particle. The results indicate that the three alumina catalysts show obvious catalytic activity for urea hydrolysis at 125 °C. The order of activity is η-Al₂O₃?>?γ-Al₂O₃?>?α-Al₂O₃, and the activity difference increases with increasing temperature. According to the characterization results, surface acidity has little impact on the activity of catalyst. However, it was found that surface basicity of alumina catalyst plays an important role in catalytic hydrolysis of urea, and the activity of catalyst may be also influenced by the basic strength. With η-Al₂O₃ as catalyst, the urea concentration in wastewater is reduced to 4.96 mg/L at a temperature of 165 °C. Moreover, the η-Al₂O₃ shows a good stability for urea hydrolysis. The hydrolysis of urea over η-Al₂O₃ catalyst can evidently reduce the reaction temperature and is promising to replace industrial thermal hydrolysis process.     

Behavior and mechanism of arsenate adsorption on activated natural siderite: evidences from FTIR and XANES analysis

Activated natural siderite (ANS) was used to investigate its characteristics and mechanisms of As(V) adsorption from aqueous solution. Batch tests were carried out to determine effects of contact time, initial As(V) concentration, temperature, pH, background electrolyte, and coexisting anions on As(V) adsorption. Arsenic(V) adsorption on ANS well-fitted pseudo-second-order kinetics. ANS showed a high-adsorption capacity of 2.19 mg/g estimated from Langmuir isotherm at 25 °C. Thermodynamic studies indicated that As(V) adsorption on ANS was spontaneous, favorable, and endothermic. ANS adsorbed As(V) efficiently in a relatively wide pH range between 2.0 and 10.0, although the removal efficiency was slightly higher in acidic conditions than that in basic conditions. Effects of background electrolyte and coexisting anions were not significant within the concentration ranges observed in high As groundwater. Results of XRD and Fe K-edge XANES analysis suggested ANS acted as an Fe(II)/(III) hybrid system, which was quite effective in adsorbing As from aqueous solution. There was no As redox transformation during adsorption, although Fe(II) oxidation occurred in the system. Two infrared bands at 787 and 872 cm^?1 after As(V) adsorption suggested that As(V) should be predominantly adsorbed on ANS via inner-sphere bidendate binuclear surface complexes.