电站锅炉袋式除尘器滤料使用寿命初探

滤料不仅影响袋式除尘嚣的使用可靠性，同时存在经营成本问题。通过实际应用的夯期试验和对试验结果的分析，确定了影响滤料使用寿命的关键技术指标，适当降低喷吹气压不仅不会影响清扫效果还对延长滤料使用寿命十分有利。     

Sampling of airborne polycyclic aromatic hydrocarbons with semipermeable membrane devices

Semipermeable membrane devices (SPMDs) are nowadays used as passive samplers of organic pollutants. The knowledge of the sampling rate values (R_S) of each substance trapped on membranes is necessary to calculate their average concentration. Here we calculate R_S values for 16 polycyclic aromatic hydrocarbons using the comparison of active sampling method results and the amounts sequestered by SPMDs at varying exposure times.Selected article from the Regional Symposium on Chemistry and Environment, Krusevac, Serbia, June 2003, organized by Dr. Branimir Jovancicevic.     

Carbon Molecular Sieving Membranes Derived from Lignin-Based Materials

Carbon molecular sieving membranes were prepared by pyrolysis of lignocresol derived from lignin by the phase-separation method. Lignocresol membranes formed by a dip process on a porous -alumina tubing were carbonized at 400–800°C under nitrogen atmosphere. The thickness of the membrane formed on the outer surface of the substrate was about 400 nm judging from SEM observation. Gas-evolving behavior of lignocresol was measured using thermogravimetry-mass spectrometry (TG-MS). The gaseous products evolved from lignocresol included a number of fragments with higher molecular weights; whereas those from phenolic resin are mainly due to phenol and methylphenol. These evolved pyrolysis fragments effectively contribute to micropore formation of carbonized lignocresol membranes. Gas permeation rates through the membrane decreased in the order of increasing kinetic molecular diameter of the penetrant gas, and the membrane behaved like a molecular sieve. The permeation properties were dependent on heating conditions, and a pyrolysis temperature of 600°C gave the best membrane performance. Gas selectivities of the membrane prepared at 600°C were 50, 8, 290, and 87 for CO₂/N₂, O₂/N₂, H₂/CH₄, and CO₂/CH₄ at 35°C, respectively.     

人工加速老化测试--氙灯试验箱

讨论两种常见的、不同类型、测试条件一致的氙灯试验箱。详述了其不同的配置对光谱、辐照度控制、过滤器类型、潮湿、湿度控制、温度控制和校准等的影响。阐述了样品安置、设备的维护保养等实际操作方面的问题以及老化测试标准。     

一体式膜-生物反应器的水动力学特性

以研究一体式膜 -生物反应器的水动力学特性为目的 ,通过试验测定了反应器中膜间液体错流流速的分布和大小 ,建立了描述错流流速的计算模型 ,并考察了曝气量和反应器结构对错流流速的影响 .曝气量为 40 m³/h时 ,膜组件中部的错流流速为0.36～ 0.4³m/s,比膜组件 2边的流速约大 6.2%～ 21%.错流流速实测值与模型计算值吻合良好 .曝气量为 20～50 m³/h时 ,错流流速随曝气量的升高而增大 ,当曝气量大于 50 m³/h后错流流速逐渐趋向平稳 ;反应器高度越高 ,上升流通道越窄、下降流道和底部流道越宽 ,在同样曝气量条件下 ,可获得越大的错流流速 .     

降低脉冲布袋除尘器可编程控制器控制设备造价的探讨

论述通过对脉冲布袋除尘器清灰电磁阀进行分组来降低脉冲布袋除尘器由可编程控制器(PLC)构成控制系统的造价的一种方法.     

针刺毡滤料的研制与应用

本文介绍了针刺毡滤料的优点、加工方法、主要工艺参数、表面整理及在环境保护中的应用。     

半经验生物滴滤器模型研究

生物滴滤(BTF)净化有机废气是一个复杂的过程,其数学模型往往形式繁琐、参数众多,实际应用比较困难.半经验生物滴滤模型是基于生物酶促反应基本原理(米-门方程),并在含苯废气的生物滴滤净化动态实验和生物膜静态实验等研究的基础上建立和完善的一个应用模型.为了符合生物滴滤器内的实际状况,在建模过程中引入了微生物质量浓度沿床层深度变化的函数等合理假设.模型的检验采用将静态实验所得参数代入模型计算,并与生物滴滤动态实验结果进行对比的方法.检验结果表明:在较宽的负荷、表观过滤气速范围内,该模型对滴滤器的模拟值均较符合实验值.该模型的数学形式简单,参数也较少,且主要参数,如生物膜最大净化速率,K值及微生物质量浓度分布等均可通过生物膜静态实验测得.      

水消毒处理中膜技术的应用

本文较全面地评述了膜技术在水消毒处理中的应用 ,包括消毒机理、效果及影响因素 ,展望了应用前景     

电渗析技术的新进展

电渗析技术是膜分离技术之一 ,由于具有高效、低能耗等特点已经被多个行业广泛使用。本文阐述了几种新的电渗析技术 ,包括无隔板电渗析、填充床电渗析、双极膜电渗析等 ,并探讨和综述其研究现状和发展前景。