颗粒粒径和含固率对疏浚泥沙絮凝沉降的影响

为保护海洋生态环境,合理利用海洋倾倒区,防止悬浮泥沙扩散,采用絮凝处理工艺,在不考虑外部环境的影响下,探讨颗粒粒径和含固率对疏浚泥沙的絮凝作用的影响;采用湿筛法对珠江口疏浚泥沙进行分组,将疏浚泥沙分为混合样、粒径>74 μm、粒径<74 μm、粒径<37 μm和粒径<15 μm的5个粒径段,研究不同粒径段和不同含固率泥沙在加入不同量聚合氯化铝 (PAC) 后,絮凝前后的粒径分布变化特征。结果表明：粒径>74 μm的泥沙颗粒不发生絮凝作用;向含固率为10%的泥沙中加入相同量的絮凝剂后,絮凝沉降速率由慢到快、沉积泥含水率由高到低、沉积泥体积由高到低的粒径段均依次为混合样、粒径<74 μm、粒径<37 μm和粒径<15 μm;对不同含固率的泥沙进行絮凝调理后,25~37 μm粒径段的粒径占比均呈现出随泥沙含固率的增大先增大后减小的趋势,当含固率为5%~10%时粒径占比最高,累积质量分数差异较大的粒径段出现在28~32 μm;对含固率为10%的泥沙进行絮凝处理后,<30 μm的粒径段,絮凝前的占比>絮凝后的占比;30~40 μm的粒径段,絮凝后的占比>絮凝前的占比;不同含固率的泥沙粒径占比峰值由23 μm分别变为33、32.8、32.1、31.6和32.2 μm,且粒径<30 μm的细颗粒含量明显减少,粒径>30 μm的细颗粒含量明显增加。综上所述,在不考虑外部环境的影响下,30 μm为该区域泥沙的絮凝临界粒径;泥沙含固率在5%~10%时,不利于PAC对泥沙的絮凝作用;絮凝后,泥沙絮团粒径为30~40 μm。本研究成果可为疏浚物海洋倾倒前环保处理技术提供关键参数和依据,并为泥沙的絮凝机理的进一步探索提供参考。     

粒径精确调控的微胶囊催化材料制备及应用

提出基于核材与壳材粒径双调控的微胶囊催化材料制备新思路,通过旋风分级和气力乳化聚合工艺优化,最终实现微胶囊的粒径调控。重点考察了气力乳化工艺参数和核材粒径、核壳材料质量比等对微胶囊平均粒径、粒径分布和包覆率的影响。实验结果表明：当气力乳化的气体流速为1.12 m·s-1时,壳材液滴的融合和乳胶粒的粘并现象均较少,聚合体系可较稳定地保持均质化壳材液滴的尺寸;在保证高包覆率的条件下,核材粒径影响着微胶囊的平均粒径,核材粒径为15.4 μm时,制备出的微胶囊平均粒径最小;核壳材料质量比对微胶囊粒径的影响明显,其为1:3.5时,微胶囊材料平均粒径为180 μm;亲水亲油平衡值（HLB）对粒径调控能力有限,平均粒径最小时微胶囊包覆率最大。通过对乳化聚合工艺和配方的综合调节,可制得一系列粒径可调范围大,粒径均一,包覆率高的微胶囊材料,应用于烟气脱硝,温度600 ℃条件下,NOx转化率可达92%。     

工艺条件对鸟粪石晶体的粒径和沉降速度的影响

采用激光粒度仪实验测定了小型套管式空气曝气填料层磷回收装置中不同条件下生成的鸟粪石晶体的体积平均粒径,考察了其变化规律,并结合Stokes公式计算了晶体的沉降速率,同时考虑鸟粪石晶体形状的影响,进行了相应的修正。实验结果表明,鸟粪石的粒径在10—200μm之间,主要集中于20～100μm;在磷回收装置中添加填料并通人空气有利于增大鸟粪石晶体的粒径和沉降速度,无填料无空气时和有填料有空气时的平均粒径分别在30～55μm和40～65μm之间。随着pH值的增大,鸟粪石晶体的粒径和沉降速度逐渐增大,但当pH大于9．0后,鸟粪石晶体的粒径和沉降速度又逐渐减小;氮磷比值从1：1增大到2：1,鸟粪石晶体的粒径和沉降速度小幅度增加,氮磷比进一步增大,鸟粪石晶体的粒径和沉降速度基本不变;镁磷摩尔比在1：1—1．2：1的范围内时,鸟粪石晶体的平均粒径和沉降速度随镁磷比的增大而增大;镁磷摩尔比大于1．2：1后,鸟粪石晶体的平均粒径和沉降速度随镁磷比的增大逐渐减小;初始磷浓度越高,鸟粪石晶体的平均粒径和沉降速度越大。     

Atmospheric particle size distributions of polychlorinated dibenzo-p-dioxins and dibenzofurans (PCDD/Fs) and polycyclic aromatic hydrocarbons (PAHs) and their implications for wet and dry deposition

Concurrent measurements of polychlorinated dibenzo-p-dioxins and dibenzofurans (PCDD/Fs) and polycyclic aromatic hydrocarbons (PAHs) in different size fractions of atmospheric particulate matter are presented for a winter and a summer sampling period. The PCDD/Fs and PAHs were primarily associated with particles of <1.35 μm aerodynamic diameter. The particle size distributions were similar for the compounds within each substance group and, surprisingly, also between the PCDD/Fs and PAHs. Changes in the particle size distribution of particle mass were reflected in the particle size distributions of the PCDD/Fs and PAHs.The data were employed to identify those particle size fractions dominating the wet and dry particle bound deposition of PCDD/Fs and PAHs and, furthermore, to assess the relative contributions of wet and dry deposition to the total particle bound deposition fluxes. The calculations indicate that coarse particles contribute most to the dry deposition while, in contrast, the wet deposition of the PCDD/Fs and PAHs is dominated by fine particles. Furthermore, it is estimated that in Bayreuth wet deposition dominates the total particle bound deposition of PCDD/Fs and PAHs.     

Simulation of the evolution of particle size distributions in a vehicle exhaust plume with unconfined dilution by ambient air

Over the past several years, numerous studies have linked ambient concentrations of particulate matter (PM) to adverse health effects, and more recent studies have identified PM size and surface area as important factors in determining the health effects of PM. This study contributes to a better understanding of the evolution of particle size distributions in exhaust plumes with unconfined dilution by ambient air. It combines computational fluid dynamics (CFD) with an aerosol dynamics model to examine the effects of different streamlines in an exhaust plume, ambient particle size distributions, and vehicle and wind speed on the particle size distribution in an exhaust plume. CFD was used to calculate the flow field and gas mixing for unconfined dilution of a vehicle exhaust plume, and the calculated dilution ratios were then used as input to the aerosol dynamics simulation. The results of the study show that vehicle speed affected the particle size distribution of an exhaust plume because increasing vehicle speed caused more rapid dilution and inhibited coagulation. Ambient particle size distributions had an effect on the smaller sized particles (approximately 10 nm range under some conditions) and larger sized particles (>2 microm) of the particle size distribution. The ambient air particle size distribution affects the larger sizes of the exhaust plume because vehicle exhaust typically contains few particles larger than 2 microm. Finally, the location of a streamline in the exhaust plume had little effect on the particle size distribution; the particle size distribution along any streamline at a distance x differed by less than 5% from the particle size distributions along any other streamline at distance x.     

工艺条件对磷回收过程中鸟粪石沉淀颗粒粒径的影响

在鸟粪石沉淀法回收废水中磷的过程中,鸟粪石颗粒的大小将直接影响其沉淀的速率,进而影响鸟粪石的沉淀效果和磷的回收率。本文采用激光粒度分析仪测定鸟粪石的平均粒径,详细考察在小型连续搅拌反应-沉淀磷回收装置中不同的工艺条件下鸟粪石颗粒粒径的变化规律,并结合Stokes公式计算鸟粪石颗粒在废水出口处的沉降速率,为沉淀池的设计提供参考依据。结果表明:鸟粪石的平均粒径在12～25μm之间,沉降速率在5.46×10-5～2.37×10-4m/s之间。随着反应室水力停留时间的延长,鸟粪石颗粒的粒径逐渐增大,当停留时间超过18 min时,颗粒的粒径基本不变;随着沉淀室水力停留时间的延长,鸟粪石颗粒的平均粒径缓慢增大,当停留时间超过70 min后颗粒粒径的变化不大;鸟粪石颗粒的平均粒径在一定程度上受废水中磷初始浓度变化的影响,在磷初始浓度为62～128 mg/L时颗粒的粒径变化不大,当磷浓度为496 mg/L时粒径有较大增加,此时鸟粪石颗粒的沉降速率也大幅度增加;鸟粪石颗粒的平均粒径受pH值的影响不大;随氮磷摩尔比的增大,鸟粪石颗粒的平均粒径略有增加;随镁磷摩尔比的增大,鸟粪石颗粒的平均粒径逐渐减小,沉降速率则有明显的下降。     

Metals leachability from medical waste incinerator fly ash: A case study on particle size comparison

This paper presents the results from a study of metals leachability of medical waste incinerator fly ash in Japan on the basis of particle size. Sequential extraction and Toxicity Characteristic Leaching Procedure (TCLP) analysis were carried out in order to quantify the leaching amount of metals in each categorized particle size. Sequential extraction was also subjected to identify the preference of binding matrix of metals. The results of sequential extraction showed an increase both exchangeable and carbonate associated chromium concentrations in the bigger particle size fractions. Likewise, concentrations of carbonate matrix of arsenic and tin tended to increase in the bigger particle size fractions. In contrast, exchangeable associated cadmium as well as both exchangeable and carbonate matrices of barium were found higher in the smaller particle size fractions. However, no correlation was found in Kendal-tau correlation analysis between particle size of the ash and metals leachability of the TCLP.     

Seasonal and particle size-dependent variations in gas/particle partitioning of PCDD/Fs

This study monitored particle size-dependent variations in atmospheric polychlorinated dibenzo-p-dioxins and dibenzofurans (PCDD/Fs). Two gas/particle partitioning models, the subcooled liquid vapor pressure (P(L)(0)) and the octanol-air partition coefficient (K(OA)) model, were applied to each particle sizes. The regression coefficients of each fraction against the gas/particle partition coefficient (K(P)) were similar for separated particles within the same sample set but differed for particles collected during different periods. Gas/particle partitioning calculated from the integral of fractions was similar to that of size-segregated particles and previously measured bulk values. Despite the different behaviors and production mechanisms of atmospheric particles of different sizes, PCDD/F partitioning of each size range was controlled by meteorological conditions such as atmospheric temperature, O(3) and UV, which reflects no source related with certain particle size ranges but mixed urban sources within this city. Our observations emphasize that when assessing environmental and health effects, the movement of PCDD/Fs in air should be considered in conjunction with particle size in addition to the bulk aerosol.     

Size Distribution of Participates Emitted from a Horizontal Spike Soderberg Aluminum Reduction Cell

Aerosol size distributions were measured in the air exhausted from a horizontal spike Soderberg aluminum reduction cell at the Kaiser Aluminum and Chemical Corporation plant in Tacoma, Wash. The particle size distributions were measured with the University of Washington cascade impactor, developed specifically for source testing. The particle mass concentrations and size distributions were found to vary significantly with changes in the cell process operations. For a typical aerosol size distribution at the exit of the cell hood the mass mean particle diameter was 5.5 microns and the particle size standard geometric deviation was 25.     

Characterization of polychlorinated dibenzo-p-dioxins and dibenzofurans in different particle size fractions of marine sediments

The distribution of polychlorinated dibenzo-p-dioxins and dibenzofurans (PCDD/Fs) was examined according to particle size in marine sediments, with a particular focus on fine particulates. Samples from different coastal sites were fractionated into five size groups (<2, 2-5, 5-10, 10-20, and 20-63 microm diameter) by gravitational split-flow thin fractionation. Despite the different size profiles and PCDD/F contents of the sediments at each site, PCDD/F levels in fractionations tended to increase as the particle size decreased; the PCDD/F levels in the finest particles were up to 16 times higher than in the coarsest particles, which was associated with their organic carbon contents. Log normalization showed high levels of PCDD/Fs in the fine silt particles (2-10 microm), which are consumable by aquatic biota. Because of the different toxicity and bioavailability of PCDD/Fs in different sediment particle sizes, it is important to study particle actions to understand their effects on the aquatic ecosystem.     

A quantitative description of vehicle exhaust particle size distributions in a highway tunnel

During the period May 18-May 22, 1999, a comprehensive study was conducted in the Tuscarora Mountain Tunnel on the Pennsylvania Turnpike to measure real-world motor-vehicle emissions. As part of this study, size distributions of particle emissions were determined using a scanning mobility particle sizer. Each measured size distribution consisted of two modes: a nucleation mode with midpoint diameter less than 20 nm and an accumulation mode with midpoint diameter less than 100 nm. The nucleation and accumulation components in some distributions also exhibited second maxima, which implies that such particle size distributions are superpositions of two particle size distributions. This hypothesis was utilized in fitting the particle size distributions that exhibited second maxima with four lognormal distributions, two for the nucleation mode and two for the accumulation mode. The fitting assumed that the observed particle size distribution was a combination of two bimodal log-normal distributions, one attributed to the heavy-duty diesel (HDD) vehicles and another attributed either to a different class of HDD vehicles or to the light-duty spark ignition vehicles. Based on this method, estimated particle production rates were 1.8 x 10(13) and 2.8 x 10(14) particles/vehicle-km for light-duty spark ignition and HDD vehicles, respectively, which agreed with independently obtained estimates.     

The size distribution of polychlorinated dibenzo-p-dioxins and dibenzofurans in the bottom ash of municipal solid waste incinerators

In this study, bottom ash was sampled from two Taiwanese municipal solid waste incinerators (MSWIs: A and B) and sieved to size classes of 4.75-9.5 mm, 2.36-4.75 mm, 1.0-2.36 mm, 0.6-1.0 mm, 0.3-0.6 mm, 0.21-0.3 mm, 0.125-0.21 mm, 0.075-0.125 mm and <0.074 mm. For both MSWIs, the major peak in the particle size distribution for the PCDD/F content was found in a particle size <0.21 mm, that is, 16.1 (A) and 4.37 pg I-TEQ/g (B). This is due to the fact that a smaller particle has higher specific surface area thus offering more adsorption sites. The mean cumulative fractions (F%) of PCDD/F I-TEQ in the bottom ash of MSWI A and B in the particle size range below 0.6, 2.36 and 4.75 mm, in sequence, are 40.4%, 77.2% and 95.6%, respectively. We suggest sieving the bottom ash before the subsequent reutilization at the suggested cut size of 0.6 mm. In the view of PCDD/Fs, bottom ash with a particle size larger than 0.6 mm, which is the more non-hazardous part, may be suitable for being the raw material of landfilling soil, road sub-base, and construction blocks. For the minus 0.6 mm fraction, vitrification with fly ash is one of the choices.     

建筑垃圾对雨水径流中Cu的吸附特性

以砖混建筑垃圾为研究对象,采用人工模拟雨水,通过静态和动态吸附实验研究了不同粒径粒级建筑垃圾对雨水径流中Cu的吸附效果。结果表明,准二级动力学模型比准一级动力学模型能更好地描述建筑垃圾对Cu的吸附过程;Freundlich等温模型能较好地拟合其等温吸附过程;不同粒径粒级建筑垃圾均对雨水径流中的Cu具有较好的净化效果,去除率均超过90%,粒径粒级越小,对Cu的净化效果越好,但其渗透性能越差;建筑垃圾的粒径粒级对Cu的吸附平衡时间、吸附速率和吸附量具有重要影响,粒径粒级2.36~4.75 mm的建筑垃圾对Cu的平衡吸附速率和平衡吸附量最大,分别为4.1 μg/min 和12.4 μg/g。     

Characterization of particulate matter concentrations during controlled indoor activities

Indoor sources have been identified as a major contributor to the increase of particle concentration in indoor environments. The work presented here is a study of the characteristics of particulate matter number size distribution and mass concentration under controlled indoor activities in a laboratory room. The objective is to characterize particulate matter concentrations indoors resulted under the influence of specific sources. Measurements were performed in an empty laboratory (period September–October 2006) using a GRIMM SMPS+C system (particle size range between 11.1 and 1083.3 nm), a DustTrak Aerosol Monitor (TSI) and a P-Trak Ultrafine Particle Counter (TSI). The studied indoor activities included candle burning, hot plate heating, water boiling, onion frying, vacuuming, hair drying, hair spraying, smoking and burning of incense stick. The AMANpsd computer algorithm was used to evaluate the modal structure of measured particle number size distribution data. Furthermore, the change of the particle number size distribution shape under the influence of different emission sources was studied versus time. Finally the particle emission rates were computed. High particle number concentrations were observed during smoking, onion frying, candle burning and incense stick burning. The highest particle mass concentrations were measured during smoking and hair spraying. The shift of the particle size distribution to larger diameters suggests the presence of strong coagulation effect during candle burning, incense stick burning, smoking and onion frying. The size distribution was mainly bimodal during onion frying and candle burning, whereas the size distribution remained unimodal during incense stick burning and smoking experiments.     

A new method for the determination of collection efficiency of an aerosol sampler by electron microscopy

A method was developed to determine the particle collection efficiency of an aerosol sampler by electron microscopy. The determination method measures the absolute concentration of particles and the particle size distribution at the sampler inlet by two aerosol samplers connected in series. Particle samples collected in each sampler were microscopically observed and analyzed by electron microscopy. By this “double-sampler method”, the particle collection efficiencies of the thermal and electrostatic precipitators were determined as a function of particle size. The average particle size ranged from 0.02 to 0.4 μm and mean collection efficiencies were found to be 72 and 79% for the thermal and electrostatic precipitators, respectively.     

Development of a measuring technique for simultaneous in situ detection of nanoscaled particle size distributions and gas temperatures

Point measurements of time-resolved LII signals have been performed in sooting premixed low pressure flames. Soot particle size distribution and gas temperature in these flames are known from independent measurements. This data is used to validate parameters of an improved LII model, where special emphasis is taken on the accurate modelling of mass and heat transfer rates. Using this model particle size distributions and gas temperatures can be estimated from time-resolved LII signals using non-linear regression. Standard numerical methods are applied. An experimental setup is presented, which allows measuring one-dimensional maps of particle size distribution and gas temperature. The technique is based on the one-dimensional and time-resolved detection of LII signals using a Streak camera.     

On the Minimum Efficiency and the Most Penetrating Particle Size for Fibrous Filters

Equations for predicting the minimum efficiency and most penetrating particle size for fibrous filters have been derived by considering the diffusion and interception mechanisms. The results show that the most penetrating particle size decreases with increasing filtration velocity and with increasing fiber volume fraction, and increases with increasing filter fiber size. The corresponding equation for minimum efficiency has also been derived showing the dependence on filtration velocity, fiber volume fraction, and fiber size. These results have been compared with experimental data and satisfactory agreement has been obtained.     

Venturi Scrubber Performance

The object of this program was to study particle collection efficiency in venturi scrubbers in order to account for the effects of particle size and wettability, venturi size, and fluid flow rates. The body of information is directed to those interested in the prediction of particle collection efficiency in venturi scrubbers.     

Precipitation of swine and cattle manure phosphorous using limestone dust

The effectiveness of SPS and PULPRO, fine limestone dusts, in precipitating swine and dairy manure phosphorous (P) was determined in the laboratory. Both manures were sieved before being treated with limestone, to reproduce the treatment of mechanically separated manure and to observe the precipitation effect of limestone without that of the large manure solid particles. P precipitation was optimized by varying precipitation conditions (propeller blade speeds, mixing time and limestone levels) and limestone particle size. P precipitation was optimized using a propeller blade mixing speed of 0.3 m s(-1) for at least 5 minutes, using 3% limestone (dry limestone mass over wet manure mass). In terms of particle size, PULPRO 20 (limestone with a particle size of 0.02 mm) produced the most P precipitation and the smallest volume and mass of sludge, as compared to PULPRO 10, PULPRO 3 and SPS (limestone with a particle size of 0.01, 0.003 and 0.3 to 0.003 mm, respectively). For both 9.5% TS (total solids) dairy and 8.8% TS swine manure, mechanical separation followed by limestone precipitation concentrated 90% of manure TS and TP in a sludge volume representing 45% of the initial raw manure mass.     

Atmospheric equilibrium model of sulfate and nitrate aerosols—II. Particle size analysis

Part I of this work presented a thermodynamic equilibrium model for the quantity, composition, and physical state of atmospheric sulfate/nitrate/ammonium aerosols. In this work we extend that model to include particle size. That is, given total nitrate and ammonium levels, relative humidity and temperature, and the distribution of sulfate by particle size, we calculate the equilibrium quantity, composition, and physical state of the aerosol as a function of particle size. The model provides an explanation for the differences in observed ambient sulfate and nitrate size distributions.