厌氧膜生物反应器处理高浓度食品废水的应用

采用由完全混合的厌氧生物反应器和板杠式超滤膜组成的膜生物反应器对高浓度食品放心水进行处理,考察了厌氧膜生物反应器的处理效果及其对负荷、水力停留时间等的稳定性,膜组件装填面积为０．６４ｍ＾２,膜材质为聚醚砚（ＰＥＳ）,膜截贸分子量为２００００。结果表明：ＣＯＤ负荷在２～３ｋｇ／（ｍ＾３．ｄ）时,膜出水ＣＯＤ去除率可达８０％～９０％,当ＣＯＤ负荷超过４．５ｋｇ（ｍ＾３．ｄ）时,混合液ＶＦＡ出现积累,Ｃ     

废旧轮胎热解过程的温度效应

通过废旧轮胎热解产物的分布研究该过程的温度效应,发现温度升高、燃料油产率增加,炭黑产率减少,即热解温度从４５０℃～５５０℃上升到６５０℃～７５０℃,燃料油产率从３３．１％～３５．４％增加到４３．２％～４５．１％,炭黑产率从４６．２％～４５．１％,炭黑产率从４６．２％～４９．２％下降为３５．１％～３７．１％,采用ＧＣ／ＭＳ分析燃料油,确定出其中仍１４０多个组分,整个油品中芳香烃化作物占了７５％以上,     

温度与湿度对氨为添加剂脉冲放电烟气脱硫的影响

对脉冲放电烟气脱硫的实验研究与理论分析表明,ＳＯ２的除主要取决于ＮＨ３与ＳＯ２热化学反应;在单位体积烟气注入能量为０－５Ｗ·ｈ／ｍ＾,脉冲放电使ＳＯ２脱率提高０－２５％,脱硫产物的主要组分是（ＮＨ２）２ＳＯ４,其含量随着单位体积烟气注入能量的增加而增大气光单位体积烟气注入能量为３Ｗ·ｈ／ｍ＾３,停留时间小于１０ｓ工业应用许可的范围内,烟气脱硫最佳温度为６０－６５℃,最佳含水体积分数为９－１１％。     

中空纤维膜生物反应器处理生活污水的特性

中空纤维膜生物反应器生活污水处理特性的试验研究结果表明：Ｄ ＨＲＴ为１．５ｈ,ＣＯＤ容积负荷为５．７６ｋｇ／（ｍ＾３·ｄ）条件下,均可实现９０％以上的ＣＯＤ去除率;对ＮＨ３－Ｎ的去除率可稳定在９０％以上,高ＭＬＳＳ浓度８０００－１００００ｍｇ·Ｌ）提供了内部厌氧环境,使膜生物反应器的Ｔ－Ｎ去除率可达５０－６０％,中空纤维生物反应器处理高效,不受冲击负荷影响,操作管理方便,其生活物反应器体积比常规生     

软煤层综放工作面注水防尘中的工艺问题

以现场注水试验和实验室实验结果为依据,分析并讨论了目前研究甚少而又对注水防尘实施,特别是在软煤层综放工作面实施很重要的工艺问题,提出了适宜的钻孔、封孔、润湿效果考察方法以及表面活性剂应用中的浓度选择、种类选择和应用的必要性评价方法     

环境中氟化物的迁移和转化及其生态效应

本文对环境中氟化物的迁移和转化及其对人体、动物、植物的污染生态效应作一简要的综述,主要包括以下几方面：１．环境中氟化物的来源及其地球化学特征;２．土－水－气－食物链中氟化物的迁移和积累与地方性氟流行病;３．土－水－气中氟的迁移和积累与植物氟毒效应;４．土－水－气中氟的迁移和积累与蚕桑氟化物污染;５．环境中氟污染的防治对策。     

应用物种敏感性分布评价敌敌畏对淡水生物的生态风险

敌敌畏是一类重要的有机磷杀虫剂,但其对水生生态的影响至今研究较少。为了评价其生态风险,构建了淡水水生生物对敌敌畏的物种敏感性分布(species sensitivity distribution,SSD)模型,在此基础上,讨论了影响SSD模型的主要因素;并分析了该模型的不确定性;推导了敌敌畏对不同类别生物的5%危害浓度HC5(hazardous concentration for 5%the species)阈值;整理收集了我国重要流域水体中敌敌畏的环境浓度;结合SSD模型计算了对淡水生物的潜在影响比例(potentially affected fraction,PAF)。结果表明:1)不同模型的选择会影响HC5的结果,且Burr III模型拟合结果较好,推导的HC5值为0.37μg·L-1;2)无脊椎动物在敌敌畏低浓度范围内的敏感性明显高于脊椎动物。甲壳类动物与昆虫和蜘蛛类相似,敏感度较高,鱼类则较低;3)应用Burr III模型构建SSD时,参数k值对HC5最为敏感,蒙特卡罗随机模拟得到HC5变化范围为0.05~40.57μg·L-1,均值为5.07μg·L-1;4)敌敌畏对我国淡水生态影响较小,PAF均低于1%,其中黄河和太湖流域敌敌畏的生态风险高于其他河流湖泊,珠江口和南海北部较低。上述研究结果为评价敌敌畏对全国不同水体水生生物的潜在生态风险提供了科学依据。     

Electro-conductive crosslinked polyaniline/carbon nanotube nanofiltration membrane for electro-enhanced removal of bisphenol A

● A crosslinked polyaniline/carbon nanotube NF membrane was fabricated. ● Electro-assistance enhanced the removal rate of the NF membrane for bisphenol A. ● Intermittent voltage-assistance can achieve nearly 100% removal of bisphenol A. ● Membrane adsorption–electro-oxidation process is feasible for micropollutant removal. Nanofiltration (NF) has attracted increasing attention for wastewater treatment and potable water purification. However, the high-efficiency removal of micropollutants by NF membranes is a critical challenge. Owing to the adsorption and subsequent diffusion, some weakly charged or uncharged micropollutants, such as bisphenol A (BPA), can pass through NF membranes, resulting in low removal rates. Herein, an effective strategy is proposed to enhance the BPA removal efficiency of a crosslinked polyaniline/carbon nanotube NF membrane by coupling the membrane with electro-assistance. The membrane exhibited a 31.9% removal rate for 5 mg/L BPA with a permeance of 6.8 L/(m²·h·bar), while the removal rate was significantly improved to 98.1% after applying a voltage of 2.0 V to the membrane. Furthermore, when BPA coexisted with humic acid, the membrane maintained 94% removal of total organic carbon and nearly 100% removal of BPA at 2.0 V over the entire filtration period. Compared to continuous voltage applied to the membrane, an intermittent voltage (2.0 V for 0.5 h with an interval of 3.5 h) could achieve comparable BPA removal efficiency, because of the combined effect of membrane adsorption and subsequent electrochemical oxidation. Density functional theory calculations and BPA oxidation process analyses suggested that BPA was adsorbed by two main interactions: π–π and hydrogen-bond interactions. The adsorbed BPA was further electro-degraded into small organic acids or mineralized to CO₂ and H₂O. This work demonstrates that NF membranes coupled with electro-assistance are feasible for improving the removal of weakly charged or uncharged micropollutants.     

Salinity exchange between seawater/brackish water and domestic wastewater through electrodialysis for potable water

● Present a general concept called “salinity exchange”. ● Salts transferred from seawater to treated wastewater until completely switch. ● Process demonstrated using a laboratory-scale electrodialysis system. ● High-quality desalinated water obtained at ~1 mL/min consuming < 1 kWh/m ³ energy. Two-thirds of the world’s population has limited access to potable water. As we continue to use up our freshwater resources, new and improved techniques for potable water production are warranted. Here, we present a general concept called “salinity exchange” that transfers salts from seawater or brackish water to treated wastewater until their salinity values approximately switch, thus producing wastewater with an increased salinity for discharge and desalinated seawater as the potable water source. We have demonstrated this process using electrodialysis. Salinity exchange has been successfully achieved between influents of different salinities under various operating conditions. Laboratory-scale salinity exchange electrodialysis (SEE) systems can produce high-quality desalinated water at ~1 mL/min with an energy consumption less than 1 kWh/m³. SEE has also been operated using real water, and the challenges of its implementation at a larger scale are evaluated.     

Electroconductive RGO-MXene membranes with wettability-regulated channels: improved water permeability and electro-enhanced rejection performance

● Electroconductive RGO-MXene membranes were fabricated. ● Wettable membrane channels were established between RGO and MXene nanosheets. ● Hydrophilic MXene reduces the resistance of water entering the membrane channels. ● Water permeance of RGO-MXene membrane is 16.8 times higher than that of RGO membrane. ● Electro-assistance can enhance the dye rejection performance of RGO-MXene membrane. Reduced graphene oxide (RGO) membranes are theoretically more conducive to the rapid transport of water molecules in their channels compared with graphene oxide (GO) membranes, as they have fewer oxygen-containing functional groups and more non-oxidized regions. However, the weak hydrophilicity of RGO membranes inhibits water entry into their channels, resulting in their low water permeability. In this work, we constructed wettable RGO-MXene channels by intercalating hydrophilic MXene nanosheets into the RGO membrane for improving the water permeance. The RGO-MXene composite membrane exhibits high pure water permeance of 62.1 L/(m²·h·bar), approximately 16.8 times that of the RGO membrane (3.7 L/(m²·h·bar)). Wettability test results and molecular dynamics simulations suggest that the improved water permeance results from the enhanced wettability of RGO-MXene membrane and increased rate of water molecules entering the RGO-MXene channels. Benefiting from good conductivity, the RGO-MXene membrane with electro-assistance exhibits significantly increased rejection rates for negatively charged dyes (from 56.0% at 0 V to 91.4% at 2.0 V for Orange G) without decreasing the permeate flux, which could be attributed to enhanced electrostatic repulsion under electro-assistance.