并行时域有限差分法的瞬态声场及其效率分析

建立了适用于二维水下目标声散射声场计算的并行FDTD计算模型,通过计算结果对入射波激励目标的作用过程进行了时域分析,从各个时刻的瞬态声场分布图可以明显看出衍射、透射和散射现象,并且能够直观地给出声场分布形态以及声波传播的物理过程。通过算例测试了其在不同数目节点机参与下的计算耗时、内存耗用、并行加速度和并行效率。分析了计算耗时、内存耗用、并行加速度、并行效率随节点数变化的关系曲线,同时还着重分析了并行效率下降的原因。     

都市型经济开发区生态化建设路径研究

总结了都市型经济开发区的类型和特点,重点分析了都市化经济开发区的生态环境质量制约性因素,提出了从产业生态化建设、土地利用生态化建设、信息现代化建设以及区域环境健康保障体系四个角度分析了生态化建设的路径体系和具体的措施。     

粘胶基活性炭纤维深度净化城市污水处理厂出水的实验研究

分别用粉状活性炭、粒状活性炭和粘胶基活性炭纤维处理污水处理厂出水,通过对水中COD、氨氮、浊度、pH值等指标进行对比实验,初步研究结果表明,活性炭纤维的吸附速率最快,达到吸附平衡所用时间最短,对水中COD吸附容量达124.6mg/g,浊度的去除率83%,但对氨氮、pH值无明显吸附效果。     

包埋活性炭聚氨酯软泡去除废水中苯酚的研究

通过对Pu-Ac吸附剂进行吸附苯酚实验,Pu-Ac吸附剂吸附25mg/L苯酚溶液时确定平衡吸附时间为12h;当pH值在6~7范围内,溶液呈弱酸性时对苯酚的去除率达到最大值;Pu-Ac吸附剂对腐殖酸的吸附去除率低于粉末活性炭;水体中含有的细颗粒泥沙含沙量在0.1~10kg/m3范围内对苯酚的吸附效果基本没有影响;Pu-Ac吸附剂经NaOH强碱溶液再生后,对苯酚的去除率保持在70%左右,可以循环利用。     

小球藻对Pb2+吸附及其亚细胞分布研究

通过溶液培养小球藻Pb2+暴露实验分析小球藻对Pb的富集以及亚细胞分布情况.结果表明:小球藻对Pb的富集总量随暴露浓度、暴露时间的增加而增加.运用差速离心法研究了小球藻中Pb在亚细胞中的分布,热力学实验与动力学实验的细胞分布结果均表明含细胞壁等残渣部分(组分I)中Pb的浓度远高于含细胞核、叶绿体、线粒体等细胞器膜系统(组分II)和可溶蛋白等细胞溶质部分(组分III)中Pb的浓度.采用动力学模型与等温线方程对实验数据进行拟合,结果表明小球藻对于Pb2+的生物吸附过程适宜用Elovich方程和二级吸附速率方程采描述,生物吸附平衡可用Langmiur等温式和Freundlich等温式来描述,小球藻对于Pb2+的生物吸附为非均相的扩散过程.     

活性污泥对有机污染物的吸附研究

通过中试试验,分析了活性污泥对污染物吸附的影响因素,并考察了活性污泥对城市污水中污染物的吸附效果.试验研究表明,污泥浓度(MLSS)、水力停留时间(HPT)和污泥龄(SRT)对活性污泥吸附污染物的效果有一定的影响,但污泥龄影响较小.在污泥质量浓度为3～5 g/L,HRT为36 min和SRT为2 d的运行参数下,活性污泥时COD,SS,TN和TP吸附效果分别为70.7%,87.7%,30.2%和72.2%.     

气箱式脉冲喷吹袋式除尘器清灰系统主要技术参数的确定

为了揭示气箱式脉冲袋式除尘器的清灰机理,应用压缩气体流动能量方程,推导出滤袋表面的反向清灰风速教学表达式;根据袋式除尘器实验模型测定的数据,得出了剥离力与粉尘剥离率之问的关系式,并在此基础上提出了清灰系统设计方法;应用气体射流理论得到了脉冲喷吹质量流量、喷吹口直径、空压机供气压力和供气量的计算公式.结果表明,在粉尘负荷一定的条件下,给定预期的剥离率,可以得到所必需的反向清灰风速和喷吹气体流量,据此可以确定清灰系统的主要技术参数.     

Regeneration of 2-amino-2-methyl-1-propanol used for carbon dioxide absorption

To improve the efficiency of the carbon dioxide cycling process and to reduce the regeneration energy consumption, a sterically hindered amine of 2-amino-2-methyl-1-propranol (AMP) was investigated to determine its regeneration behavior as a CO_2 absorbent. The CO_2 absorption and amine regeneration characteristics were experimentally examined under various operating conditions. The regeneration efficiency increased from 86.2% to 98.3% during the temperature range of 358 to 403 K. The most suitable regeneration temperature for AMP was 383 K, in this experiment condition, and the regeneration efficiency of absorption/regeneration runs descended from 98.3% to 94.0%. A number of heat-stable salts (HSS) could cause a reduction in CO_2 absorption capacity and regeneration efficiency. The results indicated that aqueous AMP was easier to regenerate with less loss of absorption capacity than other amines, such as, monoethanolamine (MEA), diethanolamine (DEA), diethylenetriamine (DETA), and N-methyldiethanolamine (MDEA).     

Electrochemical dechlorination of chloroform in neutral aqueous solution on palladium/foam-nickel and palladium/polymeric pyrrole film/foam-nickel electrodes

Electrochemical dechlorination of chloroform in neutral aqueous solution was investigated using palladium-loaded electrodes at ambient temperature. Palladium/foam-nickel （Pd/foam-Ni） and palladium/polymeric pyrrole film/foam-nickel （Pd/PPy/foam-Ni） composite electrodes which provided catalytic surface for reductive dechlorination of chloroform in aqueous solution were prepared using an electrodepositing method. Scanning electron microscope （SEM） micrographs showed that polymeric pyrrole film modified the electrode-surface characteristics and resulted in the uniform dispersion of needle-shaped palladium particles on foam-Ni supporting electrode. The experimental results of dechlorination indicated that the removal efficiency of chloroform and current efficiency in neutral aqueous solution on Pd/PPy/foam-Ni electrode could be up to 36.8% and 33.0% at dechlorination current of 0.1 mA and dechlorination time of 180 min, which is much higher than that of Pd/foam-Ni electrode.     

浅析锅炉水处理的必要性

锅炉给水不进行处理,必然导致锅炉的结垢和腐蚀。锅炉结垢使锅炉供暖效率降低,严重时可能会造成熔孔或爆管。