等离子体改性对活性炭纤维表面化学结构的影响

采用放电等离子体对活性炭纤维表面进行改性,通过改变活性炭纤维的化学官能团来强化活性炭纤维对SO2和NOx的吸附和催化作用。利用XPS、FTIR等方法对改性活性炭纤维的化学性质进行表征,研究了活性炭纤维表面官能团在等离子体改性过程中的转化规律和机理。实验结果表明:放电改性过程可以有效地向活性炭纤维表面引入有利于脱硫脱氮的含氧、含氮官能团;当电压为8kV,放电时间为5min时,放电改性活性炭纤维的效果最佳。     

活性炭纤维对氯仿气体动态吸附的研究

为了探讨活性炭纤维(ACF)对氯仿有机废气的动态吸附,考察氯仿气体流速、浓度、温度、ACF再生次数对吸附效率的影响以及滤速和压降的关系。结果表明:低浓度、低流速、低温度均有利于吸附。ACF对氯仿的吸附以物理吸附为主。提高氯仿气体滤速,气体压降增大。     

Energy reduction of a submerged membrane bioreactor using a polytetrafluoroethylene (PTFE) hollow-fiber membrane

The fiber length and packing density of the PTFE membrane element were increased. The MBR was stably operated under an SAD^m of 0.13 m³·m^-2·hr^-1. Specific energy consumption was estimated to be less than 0.4 kWh·m^-3. In this study, we modified a polytetrafluoroethylene (PTFE) hollow-fiber membrane element used for submerged membrane bioreactors (MBRs) to reduce the energy consumption during MBR processes. The high mechanical strength of the PTFE membrane made it possible to increase the effective length of the membrane fiber from 2 to 3 m. In addition, the packing density was increased by 20% by optimizing the membrane element configuration. These modifications improve the efficiency of membrane cleaning associated with aeration. The target of specific energy consumption was less than 0.4 kWh·m^-3 in this study. The continuous operation of a pilot MBR treating real municipal wastewater revealed that the MBR utilizing the modified membrane element can be stably operated under a specific air demand per membrane surface area (SAD_m) of 0.13 m³·m^-2·hr^-1 when the daily-averaged membrane fluxes for the constant flow rate and flow rate fluctuating modes of operation were set to 0.6 and 0.5 m³·m^-2·d^-1, respectively. The specific energy consumption under these operating conditions was estimated to be less than 0.37 kWh·m^-3. These results strongly suggest that operating an MBR equipped with the modified membrane element with a specific energy consumption of less than 0.4 kWh·m^-3 is highly possible.     

Preparation and Characterization of Cellulose/Polypropylene Composite Using an Oxidatively Degraded Polypropylene

In this work, an oxidatively degraded polypropylene (DgPP) was studied as a novel coupling agent for fibrous cellulose (FC)/polypropylene (PP) composite. An optimal preparation time of PP thermal oxidative degradation was 18 h at 130 °C, and the DgPP had functional groups such as γ-lactone and acid groups. The spherulite observation of the DgPP suggested miscibility for the undegraded PP. The addition of the DgPP presented the transparency improvement of FC/PP composite, and this behavior was found to be originated from the grafted DgPP, which was produced by the esterification reaction between the of FC and the DgPP. The scanning electron microscope (SEM) observation showed that the grafted DgPP coated the FC surface, and the tensile strength of the FC/PP composite increased by an appropriate amount of the DgPP addition. These results suggested that the DgPP was suitable for the coupling agent of FC/PP composite.     

活性炭纤维上4-氯酚及焦化废水尾水的O3催化氧化降解实验研究

选择YT-1000型活性炭纤维（ACF）作为催化剂，考察ACF与O₃协同作用催化降解水溶液中4-氯酚的最佳反应条件，并将该条件应用于焦化废水生物处理尾水中难降解有机污染物的催化氧化。ACF表面具有丰富的微孔结构，对4-氯酚有良好的吸附作用，在动力学上提高了其与O3反应的起始浓度，并且在ACF表面含氧、含氮等基团的催化作用下发生氧化反应，1 L浓度为100 mg/L的4-氯酚水样中投加2 g ACF反应6 min时，吸附作用对TOC的去除率为43.4%，而ACF协同O₃作用时的TOC去除率提高到72.5%，协同增效作用为67.1%；在选定的反应条件下，ACF协同O₃降解焦化废水生物处理尾水，60 min时的TOC与色度的去除率分别达到56.8%和96.3%。上述研究过程证明了吸附作用与催化作用的协同能有效降解生物过程不能降解的焦化废水中惰性有机污染物。     

C/YAG复合材料的抗烧蚀性能研究

目的对C/YAG复合材料的烧蚀性能和烧蚀机理进行研究。方法以高固相含量Y_2O_3-Al_2O_3溶胶为原料,低成本的碳纤维针刺毡为增强体,通过浸渍-干燥-热处理工艺制备C/YAG复合材料,利用SEM和XRD对烧蚀后材料的微观结构和物相组成进行分析。结果复合材料的质量烧蚀率和线烧蚀率分别为0.05g/s和0.12 mm/s。结论 C/YAG复合材料高的质量烧蚀率和线烧蚀率主要归因于氧乙炔焰高热流和强剪切力作用。烧蚀后材料的微观形貌可以分为中心区、过渡区和边缘区三个区域。其中烧蚀中心区主要受到热化学腐蚀和机械剥蚀的作用,而过渡区和边缘区主要受到热化学腐蚀和热物理侵蚀的作用。     

Optimization of the recovery of plastics for recycling by density media separation cyclones

Material recovery processes are presented as the optimum option for recycling plastic wastes as a means of recovering hydrocarbon resources. There exist a large variety of automated material recovery processes for recycling of such wastes but each with significant limitations. Of these, the separation based on differences in densities is advocated as the optimum process either for producing recycled products or preparing wastes for subsequent recovery processing.Density separation processes based on cyclone type density media separation (DMS) is presented as an important, potential method for increasing plastics recycling process capacities. It is demonstrated to have the capacity to separate a significantly larger range of particle sizes than those presently processed industrially. The mathematical relationship for the prediction of quality of typical LARCODEMS type density media separations by particle size and density as expressed by the Ecart Probable is presented.A proposed device configuration is presented for density media separation to optimize the recovery and purity of both density fractions produced. It is also suggested that to be economically viable, a large scale of operation is required for industrial plastics recycling operations recovering and producing a number of different plastics with a purity to be used as a substitute for virgin material.     

普通防电磁辐射家居服的开发

电磁辐射随时随地不同程度地影响着人类的健康,为减少其对人们日常生活的影响,需开发普通的防电磁辐射家居服。本文介绍了普通防电磁辐射家居服的生产过程和工艺,以及生产和设计过程中应注意关键问题,生产的防电磁辐射家居服防辐射性能可达20dB,足以屏蔽电脑、微波炉等家用电器的辐射。     

极近距离煤层综放开采工作面覆岩“两带”发育规律研究*

为深入研究极近距离煤层综放开采工作面覆岩“两带”的动态发育规律,采用理论推导、数值模拟和现场实测相结合的方法,分析袁店一矿824工作面覆岩“两带”的裂隙演化特征。结果表明:从岩层层向拉伸率角度,研究上覆岩层垮落带和导水裂隙带的垮落程度,考虑角度影响推导出岩层弯曲下沉边缘段变形前后的长度计算公式,根据覆岩的碎胀特征计算各岩层的最大下沉量,预测垮落带和裂隙带的范围分别为30.2~41.2 m和70.7~78.2 m;采用3DEC数值模拟分析该矿824工作面开挖后上覆岩层垮落的基本形态和裂隙分布规律,结合其应力、位移云图和监测线位移曲线的分布特征,得出垮落带和裂隙带的高度分别为32.50 m和77.25 m;采用分布式光纤应变监测系统,监测工作面前方80 m处上部顶板的受力情况,得出受采动影响的光纤应变呈起伏变化,且应变分布与地层岩性存在对应关系,得出垮落带高度约30.4 m,裂隙带高度约74.8 m,验证采用层向拉伸率和覆岩碎胀性2个方面来预测工作面覆岩“两带”高度的合理性,可为类似方面的研究与施工提供相应的技术依据。     

活性炭纤维去除水中有机微污染物的效果

采用 4种活性炭纤维 (ACF)作为吸附剂 ,对水中 CHCl₃、CCl₄、高锰酸钾指数 COD_Mn、紫外吸光值 E_UV254等有机微污染物的去除进行了初步研究 ,并与 ZJ-15型颗粒活性炭 (GAC)进行了对比 .吸附等温线的结果表明 ,ACF3对 CHCl₃的去除效果最好 ,当 CHCl₃的平衡浓度为 60μg· L^-1 时 ,ACF3对 CHCl₃的吸附容量为 212μg·g^-1 ;GAC对 CCl₄的去除效果最好 ,当 CCl₄的平衡浓度为 3μg· L^-1时 ,GAC对 CCl₄的吸附容量为 0.83μg·g^-1;GAC及 ACF1对 COD_Mn、E_UV254有较好的去除效果 ,当COD_Mn的平衡浓度为 2.5mg·L^-1 时 ,GAC及 ACF1对 CODMn的吸附容量分别为 2.16mg·g^-1 和 1.98mg·g^-1 ,当 E_UV254的平衡浓度为 0.05时 ,GAC及 ACF1对 E_UV254的吸附容量分别为 0.32 g^-1和 0.15g^-1.