模拟光伏曝气SBR除磷性能及其聚磷菌群落结构

基于村落生活污水排水、日光昼夜变化和SBR(序批式反应器)运行方式的特点及强化生物除磷所需的交替厌氧/好氧环境,采用模拟光伏曝气SBR处理生活污水,考察反应器的除磷效果及机理,并采用PCR(聚合酶链式反应)和TA克隆考察反应器内PAO(聚磷菌)的群落结构. 结果表明,反应器在12 d内成功启动,TP去除率从35.4%逐渐升至98.8%,此后TP去除率一直稳定在97%以上,出水ρ(TP)小于0.1 mg/L. 在反应段末期,反应器污泥中w(TP)达60 mg/g以上,其中w(complex-P)(complex-P为胞内聚合磷)达到55.0 mg/g,而w(EPS-P)(EPS-P为胞外聚合物结合磷)所占比例<10%,表明EPS吸附对除磷的贡献很小,除磷主要通过PAO的释磷/吸磷过程实现. 所有PAO均属于“Candidatus Accumulibacter”世系,Ⅱ型Candidatus Accumulibacter(包括Clade ⅡA-Clade ⅡD)是反应器内主要的PAO,其在3个克隆文库(d30、d60、d90)中所占比例分别为80.0%、80.0%和76.7%.      

混凝气浮及 SBR 法处理化学药剂废水的工程实践

采用混凝气浮＋SBR生化法处理某化学药剂生产企业废水,工程应用实践表明,混凝加药和气浮处理可有效去除废水中的油和非溶解性 COD ,COD 总去除率达到94．3％,出水达到企业排放要求。     

强突松软近距离煤层群石门揭煤防突技术研究

为了研究强突松软近距离煤层群石门揭煤防突技术,安全、顺利地揭煤,基于海孜矿Ⅱ32主运石门地质条件和瓦斯赋存状况,对近距离煤层群9+8煤层实施密集预抽钻孔抽采瓦斯与低压水力冲孔卸压增透相结合的措施,防治煤与瓦斯突出。结果表明:低压水力冲孔冲煤率达到4.5%;冲孔后瓦斯抽采流量为未冲孔的10倍以上;整体瓦斯抽采率达到71.7%,比以前提高了约1.6倍,卸压增透效果明显。预抽钻孔抽采后,9煤、8煤的残余瓦斯压力,分别为0.3MPa、0.22MPa,残余瓦斯含量分别为5.23m3/t、5.13m3/t,防突效果显著,可安全、顺利地揭开9+8煤层。     

三种常见混凝机理为主导条件下絮体特性研究

以模拟低浊微污染水为原水,硫酸铝[Al2 (SO4)3]为混凝剂,考察了3种常见混凝机理(电性中和、吸附架桥和网捕卷扫)为主导条件下絮体的成长过程、二维边界分形维数(Dpf)和比表面积及其与混凝效果的相关性.结果表明:吸附架桥为主导机理下絮体最大增长速率S (0.951)最快,达到稳定后絮凝指数FI最大(3.7%),二维边界分形维数Dpf最大(1.587),絮体呈块状且絮体间出现孔状间隙,比表面积介于网捕卷扫和电性中和之间[网捕卷扫(83.646m2/g)>吸附架桥(98.808m2/g)>电性中和(116.046m2/g)];FI值、S及Dpf变化与浊度去除率相关性较好,其相关系数分别达0.979、0.982和0.963,同时比表面积大的絮体吸附容量大,有机物的去除率高.     

应对气候变化——二氧化碳捕集与封存

全球气候变化问题日益严重,CO2捕集与封存(CCS)技术被看作是最有发展前景的解决该问题的技术之一。CCS技术主要包括3个环节:CO2捕集,运输和封存。首先介绍了CO2捕集技术,该技术按工艺主要分为燃烧前捕集、富氧燃烧捕集、燃烧后捕集和化学链燃烧捕集。随后介绍了CO2封存技术,该技术按封存地点可分为地质封存和海洋封存。在众多的CO2封存技术中,CO2强化采油技术由于其较高的经济效益近年来得到广泛应用。从国外、国内两个层面详细介绍了该技术的发展情况。     

矿山循环水中SO42-的脱除研究

采用吸附法、七铝酸十二钙法、石灰-氯化铝絮凝沉淀法对矿山循环水中高浓度SO24-的脱除进行研究。结果表明:单纯采用吸附法来处理废水,处理后水中的SO24-远不能达到工业用水标准;实验室制备的七铝酸十二钙对SO24-的去除效果不理想,仅为35%,也无法达到工业用水标准;采用石灰-氯化铝絮凝沉淀法处理废水时,当Al3+投加量为420mg/L,pH值为11时,去除率高达90%以上,可使废水中的SO24-质量浓度从1 800 mg/L降至200mg/L以下,完全可循环回用于矿山的选矿和采矿生产。     

PAC与PDMDAAC复合混凝剂去除高浊度水中有机氯

以聚合氯化铝(PAC)和聚二甲基二烯丙基氯化铵(PDMDAAC)为原料制备复合混凝剂,采用强化混凝的处理方法,对高浊度水体中有机氯(OCPs)以及浊度去除效果进行研究.考察了PAC-PDMDAAC复合比例、复合混凝剂投加量、水样初始浊度、慢速搅拌时间、pH值等因素对浊度和OCPs去除效果的影响,结合絮体分形维数和Zeta电位对去除效果进行验证.结果表明,复合比例对处理高浊水体中的OCPs以及浊度效果影响较大,PAC与PDMDAAC复合比例为5:1,投药量为1mL/L,慢速搅拌时间为15min时,OCPs和浊度去除率达到最佳;随着初始浊度的升高,水体中OCPs的去除率也随之增加,表明PAC-PDMDAAC复合混凝剂更适用于高浊度水中OCPs和浊度的去除;复合混凝剂与其他混凝剂相比,其最佳pH值范围较广,当pH值为4时,OCPs和浊度去除率达到最佳.利用絮体分形维数和Zeta电位两种表征手段对混凝效果进行进一步探讨,说明了实验结果的正确性.     

Performance evaluation on the pollution control against wet weather overflow based on on-site coagulation/flocculation in terminal drainage pipes

• A way for overflow control based on on-site coagulation/flocculation was proposed. • Coagulant and flocculant dose were optimized based on pollutant removal performance. • Settling time of 5 min is enough in a proper transmission distance. • Fast removal of particulate pollutants could be achieved under varied flow. The pollution caused by wet weather overflow in urban drainage systems is a main factor causing blackening an odorization of urban rivers. The conventional overflow treatment based on coagulation/flocculation in terminal drainage systems requires relatively large space and long retention time demand that makes it not applicable in crowded urban drainage systems or under heavy rains. On-site coagulation/flocculation in terminal drainage pipes was proposed in this study which was aimed to transfer the coagulation/flocculation process to the inside of pipes at the terminal drainage system to save space and reduce the retention time of the coagulation/flocculation process. The optimized dose of chemicals was studied first which was 80 mg/L of coagulant and 0.8 mg/L of flocculant. Settling for only 5 min can remove most of the pollutants at 406.5 m of transmission distance. In addition, the relation of wet weather overflow rate and concentration of pollution load on the on-site coagulation/flocculation process was investigated, which indicated that high removal of pollutant was gained at a large range of flow velocity and pollutant concentration. Finally, the study confirmed electric neutralization, bridging, and net capture as the major mechanisms in this process, and further optimization was proposed. The proposed process can reduce much turbidity, chemical oxygen demand, and total phosphorous, but hardly remove soluble ammonia and organics. This work provides scientific guidance to address wet weather overflow in terminal drainage pipes.     

离子强度对粘土和改性粘土絮凝去除水华铜绿微囊藻的影响

研究了水体的离子强度对粘土和壳聚糖改性粘土絮凝去除铜绿微囊藻的影响 .离子强度的增加有利于粘土对藻类的絮凝去除 .与一般粘土除藻相反 ,壳聚糖改性粘土却在离子强度低的条件下具有更好的除藻效果 ,是适合在湖泊 ,水库和江河等淡水 (低含盐量 )水体中应用的应急除藻技术 .当离子强度从 0.17mol/L降到 0mol/L时 ,海泡石除藻率从 90 %以上降为 70 %以下(投加量700mg/L) ,而壳聚糖改性海泡石的除藻率却从 70%左右升至 95% (投加量仅为 11mg/L) .用粘度法研究了壳聚糖改性海泡石的絮凝机理 ,发现相对低的离子强度更有利于壳聚糖分子链上阳电荷的相互排斥作用 ,有利于壳聚糖分子链的舒展 ,从而可以充分发挥架桥网捕作用 ,利于絮凝除藻 .     

Suspended solid abatement in a conical fluidized bed flocculator

With the random movement of silica gel beads in a conical fluidized bed, micro-vortices resulting from the fluidization promoted the collision and aggregation of suspended fine kaolin powders. The abatement efficiencies of the suspended fine solids under several hydrodynamic conditions were studied, and a suitable control strategy for operating the conical fluidized bed flocculators was identified. The suspended solids abatement efficiency was found to increase with increasing Camp Number and flocculation time (T), but decreased with the increase of velocity gradient (G) within the range studied in this research (165.1–189.6 s^-1). The abatement efficiencies were all more than 60% at the range of G = 165–180 s^-1 and T = 15–33 s at an initial kaolin solid concentration of 150 mg·L^-1, polymer aluminum chloride dosage of 60 mg·L^-1 and sedimentation time of 20 min. However, the formation of flocs was influenced by the liquid backmixing. Excessive backmixing caused the breakup of flocs and resulted in difficulty for the fine powders to aggregate and sediment to the reactor bottom. The results of the calculated fractal dimension and measured free sedimentation velocity of flocs obtained at different runs showed similar flocs properties, and indicated an easy control strategy for sedimentation of the flocs.