温度对生物强化除磷工艺反硝化除磷效果的影响

以处理城市污水的中试规模生物强化除磷A2/O活性污泥工艺系统为研究对象,考察了温度对系统COD去除和脱氮除磷效果的影响,特别是温度对活性污泥反硝化除磷性能的影响.结果表明,当温度从(30.9±0.8)℃降低到(9.1±0.6)℃时,A2/O系统的脱氮除磷效果显著下降,系统对TN和TP的污泥去除负荷明显下降.通过污泥反硝化除磷活性实验发现,随着温度的降低,系统中活性污泥的最大厌氧释磷速率、最大好氧吸磷速率和最大缺氧吸磷速率都降低.活性污泥中反硝化除磷菌(DPB)占聚磷菌(PAOs)总量的比例随温度降低稍有下降,但平均值仍维持在47.5％左右.用阿伦尼乌斯公式对实验结果进行拟合,得到系统中活性污泥聚磷菌厌氧释磷反应活化能Ea1为148.0 kJ· mol-1,聚磷菌好氧吸磷反应活化能Ea2为228.8 kJ·mol-1,发生在缺氧条件下反硝化除磷菌的吸磷反应活化能Ea3为315.8 kJ·mol-1.对不同温度下污泥絮体粒径分析结果表明,随温度降低,粒径分布更加集中,系统中活性污泥絮体颗粒平均粒径减小,不利于污泥絮体内部反硝化除磷缺氧微环境的形成.     

高岭土负载纳米Fe/Ni同时去除水中Cu2+和NO3-

工业废水常含有不同污染物如重金属离子和无机阴离子,而如何有效去除复合污染物就成为环境科学前沿研究的挑战性课题.这些污染物因化学性质不同而导致去除机理和途径也不同.本文采用合成高岭土负载纳米双金属Fe/Ni(K-Fe/Ni)同步去除水中Cu2+和NO-3.结果表明K-Fe/Ni能有效去除水中Cu2+和NO-3,但它们的去除效果却会相互受到影响.在Cu2+浓度为200mg·L-1时,NO-3的去除率达到42.5%;而未加入Cu2+时,NO-3的去除率仅有26.9%,说明Cu2+的存在提高了NO-3降解效率.同样,水中NO-3的存在也影响Cu2+的去除(Cu2+去除率从99.7%降到96.5%).但NO-3浓度对去除Cu2+的影响小于Cu2+浓度对NO-3的影响.通过BET比表面积、X射线衍射(XRD)、扫描电镜(SEM)、X射线能量散射(EDS)和X射线光电分析(XPS)对K-Fe/Ni表征的结果显示,反应后K-Fe/Ni的表面存在铁的氧化物、Ni0和被还原的Cu0.基于以上结果,我们发现K-Fe/Ni同步去除水中Cu2+和NO-3的机理是:高岭土负载下的纳米Fe0作为还原剂,在Ni0的催化产氢作用下将Cu2+还原成Cu0并沉积在K-Fe/Ni上而形成纳米Fe/Ni/Cu三金属催化剂,从而加速催化水中NO-3降解.     

城市污水处理厂及其受纳水体中5种典型PPCPs的赋存特征和生态风险

以5种药品及个人护理用品(pharmaceuticals and personal care products,PPCPs)包括氯贝酸、酮洛芬、萘普生、双氯芬酸和布洛芬为目标物,初步研究了它们在上海某生活污水处理厂不同污水处理单元中的赋存特征和去除特性,探讨了污水处理厂受纳河流中5种PPCPs的分布情况,并对其在受纳水体中的生态风险进行了初步评估.结果表明,5种PPCPs在污水处理厂进水中均被检出,表明生活污水是污水处理厂中PPCPs的来源之一.5种PPCPs在整个污水处理工艺中不能全部去除,微生物转化/降解是主要降解机制.受纳污水河流中5种PPCPs的分布特征与污水处理厂出水中的相似,且排污口下游水体中目标物浓度普遍高于上游,反映出污水处理厂排放可能是其受纳水体中PPCPs的主要来源之一.初步风险评估结果表明,受纳水体中双氯芬酸存在高生态风险,而酮洛芬、萘普生、氯贝酸和布洛芬的生态风险相对较低.     

高氨氮废水与城市生活污水短程硝化系统菌群比较

短程硝化是污水脱氮工艺中的重要环节,系统中的菌群结构决定了其处理效果.为探讨短程硝化系统中的微生物对不同污水的适应性,利用细菌16S rDNA克隆文库、磷脂脂肪酸(PLFA)和定量PCR分析方法对高氨氮废水和城市生活污水短程硝化系统中活性污泥的细菌群落结构、总体微生物的多样性以及功能微生物进行了比较.克隆文库结果表明两个系统中细菌群落结构明显不同,城市生活污水中细菌种类更丰富,但两个系统的优势菌群都属于变形菌门(Proteobacteria)和拟杆菌门(Bacteroidete).磷脂脂肪酸分析结果显示高氨氮废水短程硝化系统中微生物多样性指数和均匀度指数明显低于城市生活污水.定量PCR结果表明,高氨氮废水短程硝化系统中氨氧化菌(AOB)与亚硝酸盐氧化菌(NOB)的数量都多于城市生活污水短程硝化系统;高氨氮废水短程硝化系统中AOB比NOB高3个数量级,而城市生活污水短程硝化系统中AOB比NOB高2个数量级.     

发酵液作为EBPR碳源的动力学模拟

发酵液是一种优质的碳源,能够提高生物除磷系统(EBPR)的除磷效果.采用基于碳源代谢的修正ASM2模型,能够较好地模拟发酵液作为EBPR碳源的动力学变化规律.发酵液作为EBPR唯一碳源时,系统中的异养菌不仅不对聚磷菌(PAO)的生长构成竞争关系,反而促进PAO的生长.发酵液作为实际污水的补充碳源时,优化了污水中的碳源组成,创造了有利于聚磷菌生长的环境,使EBPR中聚磷菌达到微生物总量的40%以上,比实际污水作为碳源的EBPR中的PAO含量提高了3.3倍.     

Cost-performance analysis of nutrient removal in a full-scale oxidation ditch process based on kinetic modeling

A full-scale oxidation ditch process for treating sewage was simulated with the ASM2d model and optimized for minimal cost with acceptable performance in terms of ammonium and phosphorus removal. A unified index was introduced by integrating operational costs (aeration energy and sludge production) with effluent violations for performance evaluation. Scenario analysis showed that,in comparison with the baseline (all of the 9 aerators activated), the strategy of activating 5 aerators could save aeration energy significantly with an ammonium violation below 10%. Sludge discharge scenario analysis showed that a sludge discharge flow of 250–300 m3/day (solid retention time (SRT), 13–15 days) was appropriate for the enhancement of phosphorus removal without excessive sludge production. The proposed optimal control strategy was: activating 5 rotating disks operated with a mode of "111100100" ( "1"represents activation and "0" represents inactivation) for aeration and sludge discharge flow of 200 m3/day (SRT, 19 days). Compared with the baseline, this strategy could achieve ammonium violation below 10% and TP violation below 30% with substantial reduction of aeration energy cost (46%) and minimal increment of sludge production (< 2%). This study provides a useful approach for the optimization of process operation and control.     

Removal of Cu(II) from acidic electroplating effluent by biochars generated from crop straws

The removal efficiency of copper(Cu(Ⅱ)) from an actual acidic electroplating effluent by biochars generated from canola,rice,soybean and peanut straws was investigated.The biochars simultaneously removed Cu(Ⅱ) from the effluent,mainly through the mechanisms of adsorption and precipitation,and neutralized its acidity.The removal efficiency of Cu(Ⅱ) by the biochars followed the order:peanut straw char > soybean straw char > canola straw char > rice straw char a commercial activated carbonaceous material,which is consistent with the alkalinity of the biochars.The pH of the effluent was a key factor determining the removal efficiency of Cu(Ⅱ) by biochars.Raising the initial pH of the effluent enhanced the removal of Cu(Ⅱ) from it.The optimum pyrolysis temperature was 400°C for producing biochar from crop straws for acidic wastewater treatment,and the optimum reaction time was 8 hr.     

不同Fe(Ⅲ)对活性污泥异化铁还原及除磷影响研究

以SBBR反应器活性污泥作为铁还原菌菌种来源,采用兼性厌氧/严格厌氧恒温培养试验,投加不同Fe(Ⅲ)考察各条件下的异化铁还原能力同时比较对磷的去除效果.结果表明:2种条件下Fe(Ⅲ)还原能力具有较好的一致性,依次为:Fe(OH)3＞氧化铁皮＞青矿＞红矿,其中严格厌氧条件下较好.同时,除磷效果与其呈正相关,富集培养至7d,Fe(OH)3及氧化铁皮体系出水磷浓度均达到2mg/L以下,之后继续降低,最终达到0.5mg/L以下.结合异化铁还原除磷机理,可以证明,不同Fe(Ⅲ)表面吸附作用对TP的去除贡献较小,其主要作用为铁还原菌驱动下的化学沉淀去除.     

Metal loaded zeolite adsorbents for hydrogen cyanide removal

Metal(Cu,Co,or Zn) loaded ZSM-5 and Y zeolite adsorbents were prepared for the adsorption of hydrogen cyanide(HCN) toxic gas.The results showed that the HCN breakthrough capacity was enhanced significantly when zeolites were loaded with Cu.The physical and chemical properties of the adsorbents that influence the HCN adsorption capacity were analyzed.The maximal HCN breakthrough capacities were about the same for both zeolites at 2.2 mol of HCN/mol of Cu.The Cu2p XPS spectra showed that the possible species present were Cu2O and CuO.The N1s XPS data and FT-IR spectra indicated that CNwould be formed in the presence of Cu+/Cu2+ and oxygen gas,and the reaction product could be adsorbed onto Cu/ZSM-5 zeolite more easily than HCN.     

Synthesis and characterization of agricultural controllable humic acid superabsorbent

Humic acid superabsorbent polymer (P(AA/AM-HA)) and superabsorbent polymer (P(AA/AM)) were synthesized by aqueous solution polymerization method using acrylic acid (AA), acrylamide (AM) and humic acid (HA) as raw material. The effects of N,N'-methylenebisacrylamide (MBA) crosslinking agent, potassium peroxydisulfate (KPS) initiator, reaction temperature, HA content, ratio of AA to AM, concentration of monomer and neutralization of AA on water absorption were investigated. Absorption and desorption ratios of nitrogen fertilizer and phosphate fertilizer were also investigated by determination of absorption and desorption ratio of NH₄⁺, PO₄^3- on P(AA/AM-HA) and P(AA/AM). The P(AA/AM-HA) and P(AA/AM) were characterized by Fourier translation infrared spectroscopy, biological photomicroscope and scanning electron microscopy (SEM). The optimal conditions obtained were as follows: the weight ratio of MBA to AA and AM was 0.003; the weight ratio of KPS to AA and AM was 0.008; the weight ratio of HA to AA was 0.1; the mole ratio of AM to AA is 0.1; the mole ratio of NaOH to AA is 0.9; the reaction temperature was 60℃. P(AA/AMHA) synthesized under optimal conditions, has a good saline tolerance, its water absorbency in distilled water and 0.9 wt.% saline solution is 1180 g/g and 110 g/g, respectively. P(AA/AM-HA) achieves half saturation in 6.5 min. P(AA/AM-HA) is superior to P(AA/AM) on absorption of NH₄⁺, PO₄^3-. The SEM micrograph of P(AA/AM-HA) shows a fine alveolate structure. The biological optical microscope micrograph of P(AA/AM-HA) shows a network structure. Graft polymerization between P(AA/AM) and HA was demonstrated by infrared spectrum. The P(AA/AM-HA) superabsorbent has better absorbing ability of water and fertilizer, electrolytic tolerance and fewer cost than P(AA/AM) superabsorbent.