Effect of Agglomerate Size Distribution on Loose Packing Fraction

Discrete element modeling was used to establish the effects of size distribution on loose packing fraction during the fall of 5000 to 10 000 agglomerates. Monosized distributions exhibited slightly lower packing fraction than narrow distributions. However, broad distributions always produced the lowest packing fraction. The application of radius ratio rules had an effect opposite to that intended. Smaller fines had a disproportionately large effect on packing fraction, an effect attributed to gaslike behavior. Gravity-driven random packing in ceramic agglomerates was governed by a combination of bridge formation and kinetic agglomerate–agglomerate interactions, not by geometric constraints.     

氧化锆催化剂粉末粒度及粒度分布测定的研究

以水作分散介质,用激光粒度测定仪测定了氧化锆催化剂粉末粒度及粒度分布,测试方法快速、准确,测试结果令人满意。     

气相流化床聚乙烯颗粒粒径分布的定制

基于气相法聚乙烯流化床反应器颗粒粒径分布的预测[1],提出了颗粒粒径分布定制模型.通过模型的优化计算,可得到催化剂粒径及其分布、操作气速、反应温度、乙烯浓度和丁烯浓度等生产操作参数,由此进行生产可获得具有良好流态化特性的聚乙烯颗粒粒径分布,能为生产具有特定粒径分布的聚乙烯颗粒提供理论指导.模型由工业装置的生产数据分析了计算结果的合理性.最后,以三种粒径分布的聚乙烯颗粒为例讨论了模型的可行性.同时,运用粒子群优化算法求解模型的非线性规划问题,算法具有调整参数少、收敛速度快和全局优化等优点.     

激光粒度仪法测定HDPE粉末粒度及粒度分布的研究

将HDPE粉末分散在乙醇-水介质中,用激光粒度仪动态测定其粒度及粒度分布。     

分子印迹聚合物微球的粒径尺寸及分布

印迹技术是近年来发展起来的基于模拟抗体-抗原相互作用原理的新技术,广泛应用于手性物质拆分、仿生传感器、固相萃取、抗体模拟等领域。悬浮聚合法是制备分子印迹聚合物微球最常用的方法,本文就影响悬浮聚合法制备分子印迹聚合物微球粒径尺寸及分布的因素进行了探讨。     

Reformulation of an Aqueous Alumina Slip Based on Modification of Particle-Size Distribution and Particle Packing

Six alumina casting slips with particle-size distributions varying from 44 to 0.1 μm were examined. Particle packing was calculated using the approach of Andreasen. Viscosity, green density, and pore-size distribution were measured. It was found that contouring the intermediate size distribution for particles finer than 15 μm provided the most desirable viscosity for slips composed of wide size distributions. For slips containing 50 vol% solids, the lowest viscosity obtained was 196 × 10⁻³ N · s/m² (with a two-component size distribution), and a green density of 2.52 g/cm³ (65% of theoretical) was achieved with a ternary system. These casts had bimodal pore-size distributions centered around approximately 1 and 0.1μm.     

激光粒度仪分级测定水煤浆粒度分布的研究

为确定多种磨矿产品级配制得水煤浆样品的粒度分布,文章提出了分级测定水煤浆粒度的方法,已知各磨矿产品的粒度分布,通过分级拟合的方法得到不同质量比级配样品的粒度分布。结果表明:分级计算方法得到的煤样粒度分布可以准确反映出级配样品的峰型,且粒度测试结果较为准确。     

计算颗粒粒度分布的递推算法

针对光透过离心沉降法的数据处理,综合应用Stokes公式和Lambert–Beer定律,考虑了颗粒消光系数的影响和离心沉降中的径向稀释效应, 提出计算颗粒粒度分布的递推算法. 实验结果表明, 该算法计算过程简单,结果准确, 也可用于重力沉降.     

激光散射法快速测定催化剂粒度分布

采用激光粒度仪快速分析催化剂的粒度,利用激光光束对样品池内的样品颗粒进行衍射,散射光的角度与颗粒的粒度成反比,散射光的强度与颗粒的浓度成正比,所有测量由计算机分析测量并计算。该方法分析速度极快,测量范围广,操作简单、快捷,可以很好的满足对各种催化剂、粉尘的粒度分析的需要。     

颗粒堆积现象的计算机模拟

颗粒堆积现象的计算机模拟是为能经济地、有铲地分析和优化不同材料如陶瓷、水泥、医药、粉末冶金、聚合物等的性能，并为设计先进材料朝代一种行之有效的手段，近15年来该领域研究的评述表明颗粒堆积现象模拟，尤其在动态过程方面已取得了一些进展。有些计算机模拟软件已应用于模拟如陶瓷和混凝土的颗粒堆积过程，离散元方法也成功地被应用于模拟过程中。另外，为了简化现有的计算机模拟过程，有关专家用一维Monte Carlo方法来取代复杂的三维方法，同时讨论了现有的颗粒堆积过程模拟方法所存在的问题和局限性。     

乙氧基镁催化剂粉末粒度及粒度分布测定的研究

用乙醇做分散介质,用激光粒度测定仪测定四个乙氧基镁催化剂粉末试样的粒度及粒度分布,测试快速、准确。试验结果显示乙氧基镁（德国）催化剂粉末粒度最小,粒度分布集中,在四个样品中质量最好,试验结果令人满意。     

粒度测试及激光衍射粒度测试法在涂料工业中的应用

介绍了涂料工业中常用的几种测量粒度及粒度分布的方法及适用范围,并从几个方面阐述了激光衍射粒度测试法作为一种新颖的颗粒粒度测量技术在涂料工业中的应用。     

丁二烯气相聚合产物分子量分布和粒径分布模型研究

对非均相催化的丁二烯气相聚合,基于聚合物多层模型,考虑催化剂颗粒间活性位初始浓度和粒径分布对聚合物分子量分布和粒径分布的影响,建立了聚合物分子量分布和粒径分布的数学模型。模拟了反应温度、催化剂颗粒间活性位初始浓度和粒径分布等因素的影响,结果表明。随着温度升高,聚合物颗粒平均粒径变小,粒径分布变窄,聚合物分子量变小,分子量分布变宽;催化剂颗粒间的活性组分负载越均匀,聚合物分子量越大,分子量分布和粒径分布越窄;随着催化剂平均粒径变大,聚合物分子量变小,分子量分布变宽,不存在催化剂颗粒粒径分布和聚合物颗粒粒径分布间的复制现象。模型模拟结果与实验结果吻合较好,可用于预测丁二烯气相聚合产物的分子量、分子量分布和粒径分布。     

颗粒级配对高掺量粉煤灰干混砂浆性能影响的研究

依据颗粒紧密堆积理论,一般采用Andreasen方程计算粉体紧密堆积用于表征粉体颗粒的级配作用.通过研究不同粒径粉煤灰对高粉煤灰掺量干混砂浆的性能影响,研究得出:颗粒太细的粉煤灰,会更加偏离原来的紧密堆积状态,不但不能充分发挥其微观填充的补强作用,反而大大降低强度.因此,使用粉煤灰与水泥复合掺配时,特别是高粉煤灰掺量,需要考虑颗粒与颗粒之间的相互补充作用,使胶凝材料的颗粒粒径分布更趋近于紧密堆积,从而提高基体材料的密实度,保持较高干混砂浆性能.     

Packing Density of Composite Powder Mixtures

A model of particle packing in binary composite systems is developed. The effects of both inclusion surfaces and touching inclusions on the packing density are taken into account. To implement the model, a statistical approach is used to determine the number of inclusion contacts as a function of inclusion content. The statistical approach indicates that the average number of inclusion contacts is a linear function of the inclusion volume fraction, a result which agrees very well with independent computer simulations. The model suggests that the packing efficiency, defined by the ratio of the packing density to the ideal packing density (as originally derived by Furnas), is governed by the inclusion volume fraction ( f_i ) and the particle to inclusion size ratio ( r ). Good agreement is obtained between the theory and experimental literature data.     

Effects of Particle Packing Characteristics on Solid-State Sintering

Alumina compacts fabricated with different green densities and different pore size distributions were characterized and the changes of the pore characteristics during solid-state sintering were studied. A critical ratio of pore size to mean particle size for pore shrinkage was determined. Porosity in the compact could be classified into two classes: the first class contains pores smaller than the critical ratio, and the second class contains pores larger than the critical ratio. Pores belonging to a different class of porosity behaved differently during sintering. Pores larger than the critical ratio were not totally eliminated during sintering. The first class of porosity controlled the ultimate sintering shrinkage, and the second class of porosity controlled the final sintered density.     

Study of Some Variables Affecting Particle Size and Particle Size Distribution of Suspension Polymerization of Methyl Methacrylate

A laboratory reactor was designed and constructed to study the effect of both speed of agitation and a concentration of suspension stabilizer on particle size and particle size distribution during the suspension polymerization of methyl methacrylate. It was concluded that the average particle size of the prepared polymer powder is directly proportional to the speed of agitation and is inversely proportional to the stabilizer concentration. New empirical equations correlating the average particle size and the particle size distribution (PSD) were derived from the study.     

紧密堆积优化固井水泥浆体系研究进展

随着油气勘探开发工作的不断深入,低压易漏井、高压超高压井等复杂井固井对油井水泥浆性能提出了更高要求,紧密堆积优化水泥浆技术提供了新的解决途径.本文将全面介绍紧密堆积理论的相关研究成果,阐述分析了几种经典紧密堆积模型与最佳粒度分布曲线,介绍了目前研究中三种粉体堆积率测定方法;随后综述了紧密堆积理论在固井水泥浆体系尤其是低密度和高密度水泥浆体系中的应用情况;笔者通过全面总结紧密堆积优化水泥浆技术提出了自己的几点认识.随着纳微米材料的兴起,预测未来紧密堆积优化水泥浆技术会有更广泛的应用前景.     

叶蜡石粒度对玻璃熔制的影响

通过实验研究了叶蜡石粒度对玻璃熔制的影响。研究结果表明:在无法控制超细粉质量分数的生产工艺下,叶蜡石粒度并非越细越好,当粒度做到325目全通时反而会导致玻璃熔化和澄清质量变差。叶蜡石超细粉的质量分数应控制在合理的范围内,大量超细粉的存在不利于玻璃的熔化和澄清,但少量超细粉的存在并不损害玻璃的熔制。     

转炉钢渣粉粒度分布的分形特征

采用Mastersizer2000激光衍射粒度分析仪对球磨转炉钢渣粉粒度分布进行了测试,运用分形几何理论分析了钢渣粉的分形维数,探讨了分形维数与球磨时间、比表面积、特征粒径、均匀性系数及胶砂性能之间的关系.结果显示:球磨转炉钢渣粉粒度分布具有分形特征;分形维数在2.2～2.5之间,其值大小反映了钢渣粉的细度和分布宽度;分形维数越大,钢渣粉越细,粒度分布越宽;分形维数与球磨时间、比表面积、特征粒径、均匀性系数以及胶砂(w(标准水泥)∶w(钢渣)=70∶30)流动度之间存在良好的线性相关,相关系数在0.95～1之间.在本实验条件下,存在一个最佳分形维数2.41,在此分形维数下砂浆各龄期抗压强度最高.