水泥厂煤粉制备系统除尘器的选型及应用

本文介绍了煤粉制备系统含尘废气的特性及治理技术的发展与应用,并从袋除尘器类型的确定、处理风量的确定、过滤风速的选取、过滤面积的计算和除尘器规格的选取等方面介绍了煤磨袋除尘器的选型,以及FGM(M)型气箱脉冲防爆袋除尘器、MMC型脉冲喷吹防爆袋除尘器和LPMC型低阻高效防爆袋除尘器在煤粉制备系统除尘中的应用推广情况.     

水泥厂煤粉制备系统袋除尘器的选型及应用

本文介绍了煤粉制备系统含尘废气的特性及治理技术的发展与应用，并从袋除尘器类型的确定、处理风量的确定、过滤风速的选取、过滤面积的计算和除尘器规格的选取等方面介绍了煤磨袋除尘器的选型，以及FGM（M）型气箱脉冲防爆袋除尘器、MMC型脉冲喷吹防爆袋除尘器和LPMC型低阻高效防爆袋除尘器在煤粉制备系统除尘中的应用推广情况。     

矿渣粉磨系统袋式除尘器的选型及应用

介绍了矿渣粉磨系统含尘废气的特性、国内治理技术现状和除尘新技术，并从处理凤量的确定、袋式除尘器类型的确定、过滤风速的选取、过滤面积的计算、除尘器规格的选取等方面介绍了矿渣粉磨袋式除尘器的选型，以及FGM型矿渣用气箱脉冲袋式除尘器和KDMC大型低阻袋式除尘器在矿渣粉磨系统除尘的应用推广情况。     

针刺毡复合滤料的性能研究

本文对针刺毡复合滤料的过滤效率、过滤阻力和过滤风速等性能指标的研究现状进行了分析,并通过实验对五种针刺毡复合滤料进行了性能比较,以供实际选用时作参考。     

窑头篦冷机除尘系统改造技术探讨

分析了广州市珠江水泥有限公司的窑头电除尘改造为袋式除尘的成功案例。指出在设计和使用上,要控制好过滤风速、气流上升速度、净气室的风速、喷吹压力、脉冲时间和周期,以及气流分布等主要技术指标,袋式除尘器阻力可大幅度下降,除尘效率可大幅度提高。     

浅谈水泥厂立窑袋除尘器的选型及应用

介绍了立窑烟气的特性及治理技术的发展与应用,并从袋除尘器类型及处理风量的确定、过滤风速的选取、过滤面积的计算、除尘器规格的选取等方面介绍了立窑袋除尘器的选型要点;介绍了LFEF型立窑袋除尘器、LMC低压长袋脉冲立窑袋除尘器和GMC型高温高压脉喷立窑袋除尘器在水泥行业的推广情况及应用效果。     

LCM型长袋脉冲除尘器

由浙江洁华环保科技有限公司开发、浙江省环境保护局推荐的LCM型长袋脉冲除尘器，适用于电力、冶金、化工、建材及垃圾焚烧行业废气净化。主要技术内容一、基本原理利用布袋过滤除尘机理，除去含尘气体中的粉尘。当含尘气体从下部锥体进入除尘器，粉尘被阻留在滤袋表面上，经过滤的净气进入上气箱，经排风管排出。随过滤工况的进行，滤袋阻力升高，由自动控制仪控制脉冲阀、离线阀、进行逐室逐排脉冲清灰，使滤袋恢复过滤能力。二、技术关键离线脉冲喷吹技术，克服了粉尘“再吸附”现象，提高了清灰效果，降低设备阻力达到长滤袋（为传统…     

滤袋表面过滤风速对粉尘排放浓度的影响

文章研究了滤袋表面过滤风速对粉尘排放浓度的影响,粉尘排放浓度与过滤风速的平方成正比,降低滤袋表面过滤风速可有效降低粉尘排放浓度。     

常规滤料与覆膜滤料的性能测试与对比

本文对常规滤料和覆膜滤料的过滤机理、过滤效率、过滤阻力等性能指标进行了测试与对比分析,指出了覆膜滤料相对于常规滤料的一系列优点,并预测了覆膜滤料的应用前景。     

电除尘器内臭氧产生规律实验研究

静电除尘器是一种工业除尘技术,但它的高压电源在使用中会产生臭氧,可能会对后续设备及材料造成一定的影响,研究臭氧产生规律对静电除尘器的安全使用有一定的指导意义。本文通过建立电除尘器的物理模型,以实验手段研究了电除尘器中臭氧产生与电压、风速、箱体位置的规律。结果表明,静电除尘器会产生臭氧,且臭氧浓度随着电压的增大而增大,随着风速的增大而减小,沿气流流动方向臭氧浓度逐渐增大,臭氧浓度与电压和风速成近似线性关系。     

袋式除尘用滤料集尘性能的冷态测定及分析

对袋式除尘常用的针刺毡、基布覆膜、梯度针刺毡三类滤料进行集尘状况下压力损失冷态实验测试。结果表明:清洁滤料压力损失由大到小分别为基布覆膜滤料、梯度针刺毡、常规针刺毡;清洁滤料的压力损失与过滤速度呈正比线性变化关系,集尘后与过滤时间、粉尘负荷呈正比二次方变化关系,并通过分析给出滤料在不同集尘负荷下阻力与过滤风速、粉尘负荷间的计算关系。     

燃煤电厂锅炉袋除尘器用PPS滤料失效原因分析

分析了燃煤电厂锅炉袋式除尘器用聚苯硫醚(PPS)破损滤袋样品的性能,并与新袋样品进行对比,得出工况含氧量、SOX浓度偏高,且有结露现象为滤袋破损的主要原因。     

铁合金电炉烟尘治理技术分析

本文在分析了半封闭铁合金电炉产生的烟气、烟尘的特性和各种除尘设备性能的基础上，提出了净化铁合金电炉烟尘的三种技术：袋式除尘、强化湿式除尘和文丘里除尘器。并对袋式除尘工艺和Calvert洗涤器除尘工艺作了介绍，分析了它们的经济技术指标。半封闭铁合金电炉烟尘只能采用布袋除尘器净化，只有那些建在环境空气质量三类区的铁合金电炉，当资金非常紧缺时，才可采用Cavlert洗涤器除尘。     

Performance of a stratified sand filter in removal of chemical oxygen demand, total suspended solids and ammonia nitrogen from high-strength wastewaters

A stratified sand filter column, operated in recirculation mode and treating synthetic effluent resembling high-strength dairy wastewaters was studied over a 342-d duration. The aim of this paper was to examine the organic, total suspended solids (TSS) and nutrient removal rates of the sand filter, operated in recirculation mode, under incrementally increasing hydraulic and organic loading rates and to propose a field filter-sizing criterion. Best performance was obtained at a system hydraulic loading rate of 10 L m(-2) d(-1); a higher system hydraulic loading rate (of 13.4 L m(-2) d(-1)) caused surface ponding. The system hydraulic loading rate of 10 L m(-2) d(-1) gave a filter chemical oxygen demand (COD), TSS, and total kjeldahl nitrogen (TKN) loading rate of 14, 3.7, and 2.1 g m(-2) d(-1), respectively, and produced consistent COD and TSS removals of greater than 99%, and an effluent NO(3)-N concentration of 42 mg L(-1) (accounting for an 86% reduction in total nitrogen (Tot-N)). As the proportional surface area requirement for the sand filter described in this study is less than the recommended surface area requirement of a free-water surface (FWS) wetland treating an effluent of similar quality, it could provide an economic and sustainable alternative to conventional wetland treatment.     

Air classification of blast furnace dust collected in a fabric filter for recycling to the sinter process

Totally dry cleaning has become a common technology for top gas cleaning in blast furnaces in recent years. A significant advantage of totally dry gas cleaning is that the dust collected is obtained as dry powder, thus simplifying the recycling of the dust in the sinter plant and avoiding aqueous emissions. The concentration of some heavy metals, especially zinc, in the collected dust is usually higher than the maximum tolerable concentration for recycling to the sinter process. Therefore, a process for separation of dust with a low level of contamination from the rest is necessary to make partial recycling possible. This is possible because the limited components are more volatile and accumulate in the finer dust fraction. In wet blast furnace top gas cleaning, hydrocyclones are well established for this separation. For the separation of dry powder from the dry dedusting process air classification can be used. Dust from the top gas of a blast furnace with a fabric filter for dry top gas cleaning was split into several size fractions using a laboratory air classifier. The concentration of Ca, Cd, Cl, Cu, Fe, K, Na, Pb and Zn was analysed for each particle class and the loss on ignition was determined. A strong dependence of the concentration on the particle size was found for the more volatile metals, whereas the Fe and Ca concentration and the loss on ignition were quite evenly distributed. With the calculated recovery–removal-functions the possible recycling rate can be estimated for a given removal rate for the limited components.     

Flow-through rates and evaluation of solids separation of compost filter socks versus silt fence in sediment control applications

Soil loss rates from construction sites can be 1000 times the average of natural soil erosion rates and 20 times that from agricultural lands. Silt fence (SF) is the current industry standard used to control sediment originating from construction activities. Silt fences are designed to act as miniature detention ponds. Research has indicated that SF sediment filtering efficiency is related to its ability to detain and pond water, not necessarily the filtration ability of the fabric. Design capacity and spacing is based on flow-through rate and design height. In addition, increased detention of runoff and pressure from ponding may increase the likelihood of overtopping or failure of SF in field application. Testing was conducted on compost silt socks (SS) and SF to determine sediment filtering efficiency, flow-through rate, ponding depth, overtopping point, design height, and design capacity. Results indicate flow-through rate changes with time, as does ponding depth, due to the accumulation of solids on/in the sediment filters. Changes in depth with time were a linear function of flow rate after 10 min of flow, up to the time the sediment filter is overtopped. Predicting the capacity of SF and SS to handle runoff without the filter being overtopped requires consideration of both runoff rate and length of runoff time. Data show SS half the heights of SF were less likely to overtop than SF when sediment-laden runoff water flow rates are less than 1.03 L(-1) s(-1) m(-1) (5 gpm/ft, gal per minute per lineal foot). Ponded depth behind a 61.0-cm (24 in) SF increased more rapidly than behind a 30.5-cm diam. (12 in) SS, and at the end of the thirty minutes, the depth behind the SF was 75% greater than that behind the SS. Removal of solids by the SF and the SS were not shown to be statistically different. Results were used to create a Microsoft Excel-based interactive design tool to assist engineers and erosion and sediment control planners on how to specify compost SS relative to SF in perimeter sediment control applications.     

棉织品的生命周期评价

生命周期评价（LCA）是ISO14000管理体系的重要组成部分，本文将棉捉品生命周期的四个阶段对环境的影响分别进行了评估，并将结果汇总计算，比较分析了在棉织品生命周期中，对环境影响最大的阶段，从而为棉织品的生态设计提供了依据。     

炼油污水深度处理回用的中试

采用两级曝气生物滤池和多介质滤池相串联的中试装置,连续处理某炼油厂污水车间二浮出水,主要考察了中试装置对污水中主要污染物的去除效果和规律,并确定了适宜的气水比。试验结果表明:采用该工艺时,除石油类外,其它各项指标都达到《循环冷却水用再生水水质标准》(HG/T3923-2007)要求的水质指标;两级曝气生物滤池的气水比分别选用5.6∶1和5∶1为宜;验证了BAF是通过生物氧化和过滤两种作用来去除COD,第一段BAF以去除污水中碳化有机物为主,第二段BAF主要以去除污水中的NH4+-N为主。     

Use of industrial byproducts to filter phosphorus and pesticides in golf green drainage water

Golf courses are vulnerable to phosphate (PO) and pesticide loss by infiltration of the sandy, porous grass rooting media used and through subsurface tile drainage. In this study, an effort was made to remove PO, chlorothalonil, mefenoxam, and propiconazole in a golf green's drainage water with a filter blend comprised of industrial byproducts, including granulated blast furnace slag, cement kiln dust, silica sand, coconut shell-activated carbon, and zeolite. To test this filter media, two 6-h storm events were simulated by repeat irrigation of the golf green after PO and pesticide application. Drainage flows ranged from 0.0034 to 0.6433 L s throughout the course of the simulations. A significant decrease in the chlorothalonil load for the experimental run (with filter media) was observed compared with the control (without filter media) ( < 0.05). In general, percent reductions in chlorothalonil were very high (>80%) near peak flows. In contrast, filter media was not effective in removing PO, mefenoxam, or propiconazole ( > 0.05). Instead, it appears that the filter blend added PO to the effluent above flow rates of 0.037 L s. Overall, flow rate, the amount of filter media used, and contaminant properties may have influenced the filter media's ability to remove contaminants. More research is needed to determine the optimal blend and configuration for the filter media to remove significant amounts of all contaminants investigated.     

KALMAN FILTER CALCULATION OF SAMPLING FREQUENCY WHEN DETERMINING ANNUAL MEAN SOLUTE CONCENTRATIONS

ABSTRACT: A linear filter (Kalman filter) technique was used with a Streamflow-concentration model the minimize surface water quality sampling frequencies when determining annual mean solute concentrations with a predetermined allowable error. The Kalman filter technique used the stream discharge interval as a replacement for the more commonly used time interval. Using filter computations, the measurement error variance was minimized within the sample size constraints. The Kalman filter application proposed here is applicable only under several conditions including: monitoring is solely to estimate annual mean concentration; discharge measurement errors are negligible; the Streamflow-concentration model is valid; and monthly samples reflect the total variance of the solute in question.