水热改性棉铃壳对水中氟的吸附

采用水热法制备了改性棉铃壳吸附剂,通过比表面积分析仪、扫描电镜和红外光谱仪表征了棉铃壳改性前后表面结构和官能团变化,并通过批实验分析了改性棉铃壳对水中F-吸附动力学及热力学特征,考察了温度、pH对吸附性能的影响。结果表明,磷酸水热改性后棉铃壳比表面积为121.7 m2/g,是改性前的18.5倍;通过水热改性可以减少酸性基团数量,有利于吸附阴离子。氟离子吸附实验结果显示,吸附反应符合准二级动力学模型,Langmuir模型能更好地描述反应的单分子层吸附特征,分离因子R L在0~0.5之间。改性棉铃壳对F-的吸附属于自发进行的吸热反应。     

Eu掺杂ZnO光催化剂降解制药废水

以醋酸锌(Zn(CH3COO)2)和六水合硝酸铕(Eu(NO3)3·6H2O)为主要原料,氢氧化钠(Na OH)为沉淀剂,聚乙二醇(PEG2000)为矿化剂,柠檬酸为p H调节剂,采用水热法制备Eu掺杂Zn O复合纳米棒光催化材料粉体。用制备的粉体对制药废水进行光催化降解实验,并研究了反应温度、反应时间、光照条件和掺杂比对其光催化氧化效果的影响。用XRD、TEM和EDS等测试手段对粉体进行了表征。研究结果表明,水热反应温度为160℃,时间为6 h,制备的3%Eu掺杂Zn O复合纳米棒光催化材料的光催化效果较好,在365 nm的紫外灯照射下150 min后,制药废水的脱色率达38.8%,COD的降解率达57.5%。     

纳米片自组装原位N掺杂(BiO)2CO3分级微球的可控合成及其优异可见光催化性能

以二氰二胺和柠檬酸铋为原料,采用一步水热法合成原位N掺杂(BiO)2CO3纳米片自组装分等级微球结构。采用XRD、SEM、XPS、FT-IR、UV-Vis DRS和PL等对合成的材料进行表征,结果表明,不同二氰二胺加入量会对(BiO)2CO3的形貌结构、禁带宽度以及电子-空穴复合率产生显著影响。二氰二胺在水热过程水解柠檬酸铋,同时N原子原位掺杂进入(BiO)2CO3晶格。N掺杂使(BiO)2CO3的光响应范围大幅拓展至可见光,通过价带XPS获得了掺杂N元素减小(BiO)2CO3禁带宽度的证据。在可见光照射下,原位N掺杂(BiO)2CO3分等级微球结构表现出对液相罗丹明B和气相NO优异的可见光催化降解活性,高于N掺杂TiO2和C掺杂TiO2。研究结果对拓展N掺杂作用向非TiO2体系的转变具有重要意义。     

Temporal evolution in PPCP removal from urban wastewater by constructed wetlands of different configuration: a medium-term study

Pharmaceuticals and personal care products (PPCPs) are widely distributed in urban wastewaters and can be removed to some extent by constructed wetlands (CWs). The medium-term (3-5 years) behaviour of these systems regarding PPCP removal is still unknown. Seven mesocosm-scale (1 m²) CWs of different configurations were operated outdoors for 39 months under the same conditions to assess their PPCP removal ability and temporal evolution. CWs differed in some design parameters, namely plant presence, species chosen (Typha angustifolia vs Phragmites australis), flow configuration and presence/absence of gravel bed (floating macrophytes surface flow, FM-SF; free-water surface flow, FW-SF; free-water subsurface flow, FW-SSF; or conventional horizontal subsurface flow, SSF). PPCP efficiencies decreased throughout time and performance differences among CWs disappeared with the systems aging. This could be due to a homogenization process in the systems caused by detrimental factors like saturation, clogging and shading. Winter efficiencies were lower than summer ones for salicylic acid, caffeine, methyl dihydrojasmonate, galaxolide and tonalide, and seasonal biological activities seem key factors to explain this fact. Maximal removal efficiencies were achieved in an unplanted-FW-SSF for ketoprofen (47-81%), naproxen (58-81%) and salicylic acid (76-98%); in an unplanted-SSF for caffeine (65-99%); in a Phragmites-FM-SF for ibuprofen (49-96%) and diclofenac (16-68%); in a Typha-FM-SF for carbamazepine (35-71%); and in a Typha-FW-SSF for methyl dihydrojasmonate (71-96%), galaxolide (67-82%) and tonalide (55-74%). Photodegradation could be involved in ketoprofen, naproxen, ibuprofen and diclofenac removal. Carbamazepine and diclofenac were moderately removed by the most efficient CWs studied. Carbamazepine might be eliminated by vegetal uptake.     

油气田水合物形成机理及抑制剂的研究进展

通过介绍水合物的结构、形成机理及形成这种物质所带来的弊端,指出了研究合理的水合物抑制剂,在油气田发展环境保护中具有重要的理论和现实意义。同时根据水合物生成条件及主要防治措施,针对现有水合物抑制剂的种类及应用特点,提出了油气田水合物抑制剂研究的发展方向。     

新型可见光催化剂BiVO4降解中成药制药废水

以Bi(NO3)3.5H2O和NH4VO3为原料,采用水热法制备了新型可见光BiVO4催化剂,并用X-射线衍射(XRD)、扫描电子显微镜(SEM)、红外光谱(IR)和紫外-可见光漫反射光谱(UV-vis DRS)对产品进行了结构表征,并将其应用于光催化降解中成药制药废水降解反应中,通过正交实验和单因素分析,考察了催化剂用量、空气流量、溶液pH值和助氧化剂H2O2对制药废水COD去除率、脱色率的影响。实验结果表明,水热产品属于单斜晶系BiVO4,其带隙能为2.41 eV,并具有良好的可见光催化活性。对于经10倍稀释的制药废水,BiVO4添加量为2 g/L,通氧量为120 L/h,助氧化剂H2O2添加量为1 mL,不改变废水pH值,在400 W金属卤化物灯离液面11 cm照射反应180 min的条件下,制药废水的COD去除率为94.3%,脱色率为95.6%,得到了较好的降解。     

湿热处理餐厨废弃物不饱和脂肪酸

为了研究湿热水解技术对餐厨废弃物中脂类物质的影响,促进餐厨废弃物的资源化处理利用,通过实验研究,分析了餐厨废弃物固相中油酸、亚油酸、α-亚麻酸和花生四烯酸4种不饱和脂肪酸在90～140℃湿热条件下处理随时间的变化规律。结果表明：实验所取餐厨废弃物经湿热处理后固相中油酸和亚油酸的含量相对较高,约为30％,花生四烯酸的含量较低,约为0．3％,随着加热时间延长,亚油酸在湿热环境下发生化学分解,其含量不断降低,而花生四烯酸的含量显著增加。当加热温度为100～120℃,加热时间为30-60min时,餐厨废弃物脂类含量比较稳定,作为适宜的湿热处理条件。值得注意的是,湿热处理后的餐厨废弃物中花生四烯酸的含量只约为0．3％,不能满足饲料标准中2％的要求。     

湿热老化后膨胀型钢结构防火涂层导热系数数值计算

通过对已有多孔材料导热系数计算模型的总结和分析,提出了湿热老化后膨胀型钢结构防火涂层导热系数的计算模型。为考察该模型的计算精度,进行了湿热老化试验及隔热性能试验,测量涂层膨胀倍率、炭化层泡孔尺寸和钢板温度等数据。结果显示,湿热老化后炭化层泡孔尺寸增大导致涂层导热系数增大,隔热性能下降,钢板温度上升。利用本文试验测量数据(泡孔尺寸)计算炭化层导热系数,再根据炭化层导热系数的数值计算结果分析钢板温度,并将钢板温度的计算结果与试验结果进行对比,两者吻合良好,验证了膨胀型防火涂层导热系数计算模型的适用性。     

水热法表面改性陶粒及其对水中磷的吸附性能

采用水热法制备碳改性陶粒和铁/碳改性陶粒,对改性陶粒表面进行了表征,研究了改性陶粒对废水中磷的吸附效果。表征结果显示,改性后陶粒形貌更规则,比表面积增加,有机官能团种类增多。吸附实验结果表明,碳改性陶粒和铁/碳改性陶粒在初始磷质量浓度为5 mg/L、pH分别为6和5、陶粒投加量为0.03 mg/L的条件下,于35℃下吸附8 h,磷的去除率分别达到97.28%和93.10%,剩余磷质量浓度分别为0.136 mg/L和0.345 mg/L;Langmuir等温吸附模型和准二级动力学方程更适合描述两种改性陶粒对磷的吸附过程,且改性后陶粒均具有良好的解吸能力,解吸率随解吸剂浓度的增加而增大。     

Pulsed pumping process optimization using a potential flow model

A computational model is applied to the optimization of pulsed pumping systems for efficient in situ remediation of groundwater contaminants. In the pulsed pumping mode of operation, periodic rather than continuous pumping is used. During the pump-off or trapping phase, natural gradient flow transports contaminated groundwater into a treatment zone surrounding a line of injection and extraction wells that transect the contaminant plume. Prior to breakthrough of the contaminated water from the treatment zone, the wells are activated and the pump-on or treatment phase ensues, wherein extracted water is augmented to stimulate pollutant degradation and recirculated for a sufficient period of time to achieve mandated levels of contaminant removal. An important design consideration in pulsed pumping groundwater remediation systems is the pumping schedule adopted to best minimize operational costs for the well grid while still satisfying treatment requirements. Using an analytic two-dimensional potential flow model, optimal pumping frequencies and pumping event durations have been investigated for a set of model aquifer-well systems with different well spacings and well-line lengths, and varying aquifer physical properties. The results for homogeneous systems with greater than five wells and moderate to high pumping rates are reduced to a single, dimensionless correlation. Results for heterogeneous systems are presented graphically in terms of dimensionless parameters to serve as an efficient tool for initial design and selection of the pumping regimen best suited for pulsed pumping operation for a particular well configuration and extraction rate. In the absence of significant retardation or degradation during the pump-off phase, average pumping rates for pulsed operation were found to be greater than the continuous pumping rate required to prevent contaminant breakthrough.