流化床喷雾造粒颗粒强度的影响因素研究

颗粒强度作为流化床喷雾造粒产品的重要评价指标,对其影响因素的实验研究具有重要的现实意义。本文在一间歇锥形流化床喷雾造粒器中,以食用小麦淀粉为原料,以明胶的水溶液为粘结剂,实验研究了流化气速、床层温度、喷嘴雾化空气压力、粘结剂浓度对喷雾造粒颗粒强度的影响。结果表明,在本实验范围内,流化气速对颗粒强度的影响显著,床层温度、粘结剂浓度对颗粒强度也有较大的影响,而且均是非单调的。但喷嘴雾化空气压力与颗粒强度之间存在正向相关性。     

窄粒度分布粉体产品分级的影响因素

在粉体制备的实际生产过程中，分级机是保证产品质量的重要环节，特别是在微粉窄级别物料的生产中尤为重要。这是因为窄级别物料要求产品的粒度分布很窄，即不能有大颗粒的存在，细颗粒含量也不能过多。这就要求分级机不但能去除物料中的大颗粒，而且要控制物料中的细颗粒...     

大豆蛋白液喷雾场粒度分布变化

目的研究大豆蛋白液喷雾场粒度分布的变化规律,为选择一个合适的蔬菜纸喷涂面提供实验数据,以期得到质量好的蔬菜复合纸覆膜。方法将大豆蛋白喷涂雾化场网格化,使用粒度仪分别测量各个区域的粒径和粒度占比分布。结果雾化场轴向距离从H=10 cm处的95μm左右,到H=15 cm处的85μm左右,到H=20 cm处的65μm左右,再到H=30 cm处的45μm左右,最大粒径占比范围逐渐降低;雾化场径向距离从L=4 cm处的40~50μm,到L=8 cm处的35~40μm,到L=12 cm处的35~40μm,再到L=16 cm处的30~35μm,最大粒径占比范围也逐渐降低;在相同的喷涂气压、喷涂液压下,随着轴向距离的增加,大豆蛋白液液滴粒径分布范围的减小,大粒径大豆蛋白液液滴的比例逐渐减少,粒径分布朝着小粒径方向靠拢,大豆蛋白液液滴粒径分布曲线越来越陡峭;在喷涂气压、喷涂液压不变的情况下,仅仅改变大豆蛋白液的粘度,在相同的喷雾场位置随着大豆蛋白液粘度的减小,粒度分布朝小粒径方向靠拢,小粒径大豆蛋白液液滴比例逐渐减小。结论喷涂气压越大、大豆蛋白液粘度越小,雾化效果越好,而喷涂液压对雾化效果影响不大;大豆蛋白液喷雾场液滴的粒径分布随着喷雾贯穿距离的增加,小粒径液滴所占比例逐渐增加,粒径分布曲线朝小粒径方向发展,同时随着垂直与喷雾轴心线径向距离的增加,小粒径液滴所占百分比也增加,粒径分布曲线朝着小粒径方向发展。     

SiC喷雾造粒粉的影响因素研究

通过SiC喷雾造粒试验,分析了影响SiC造粒粉性能的因素,如进出口温度、浆料的固含量、喷雾压力及进料速度等;同时总结出了喷雾造粒时的合理工艺,制备出了松装密度为0.91 g/cm3,流动性为20 s(样品量为30 g),且粒形较好、适于成型的SiC粉体。     

喷动流化床喷雾造粒过程实验研究

为了研究喷雾造粒过程中影响颗粒粒径生长速率的因素,本文中在自建的喷动流化床上,以玻璃珠为晶种,工业级碳酸钾溶液为涂敷液,对流化气速、喷动气速、床层温度、溶液流量和浓度等因素对颗粒生长速率的影响进行了实验研究。实验结果表明,颗粒的生长速率随流化气速、喷动气速、床层温度的增大先增大后减小;随溶液浓度、流量的增大而增大。     

喷雾造粒ZrO2粉料坯体性能的研究

以喷雾造粒 ＺｒＯ_２粉料为研究对象,通过对粉料的压力－密度曲线及坯体的 ＳＥＭ显微结构分析,发现喷雾造粒粉料的粒度分布对坯体密度的影响较小;颗粒强度的大小是获得均匀的坯体结构的关键,颗粒的强度与其大小及环境湿度有关,因此颗粒适当的增塑及去除大颗粒均有利于坯体显微结构的改善．     

Mastersizer 2000型激光粒度仪技术参数对粒度分布的影响

根据英国马尔文Mastersizer 2000型激光粒度仪的特点,探讨不同技术参数对样品粒度分布测试结果的影响。结果表明,影响样品粒度分布的主要参数为样品量(检测遮光度)、采集时间、循环速度、检测光源波长、反演光学模型及数学模型等;对于状态不明确的未知样品,应借助其他检测技术进行样品状态表征后,选择合理的光学模型和数学模型进行粒度测试。     

激光粒度仪测定煤粉粒度及分布的方法研究

采用激光粒度分析仪对具有粘附特性的3种煤粉的粒度及其粒度分布的测试方法进行了研究,以获得最佳测试效果;分别研究样品浓度、吸收率和折射率、表面活性剂、进样器泵转速以及超声时间等因素对煤粉粒度测量结果的影响。结果表明:表面活性剂和进样器泵转速对煤粉的测定结果影响较大,泵转速为1 800~2 600 r/min,加入约3 mL无水乙醇作表面活性剂时测量结果重复性好,数据比较准确。     

粉体粒度分布的分形研究

本文应用分形几何理论，研究了粉体的粒度分布特征，发现在双对数坐标下，许多材料粒径的重量累积百分含量与粒径之间呈直线关系，表明其粒度分布具有分形结构。分维可作为描述粉体粒度分布特征的一个序参量，其大小反映了粉体颗粒的组细程度和集中、不均匀特征，即粉体粒度分布空间结构性。并在监控粉磨机械效率、估测颗粒级配等方面有重要意义。     

粉体粒度分布的分形特征

应用分形几何理论，研究了粉体的粒度分布特征，发现在双对数坐标下，许多材料粒径的重量积百分含量与粒长之间呈直线关系。表明其粒度分布具有分形结构，分维可作为粒度分布特征的一个序参量，它反映了粉体颗粒的粗细程度和集中、均匀特性。     

应用激光粒度分析仪测定油田碎屑岩粒度分布

针对MSS型激光粒度分析仪在实际应用过程中存在的问题,进行了方法改进。结果表明,为了使粒度分级格式符合石油行业标准的要求,对于宽范围的碎屑岩,采用激光干湿法结合或者筛析法与激光湿法结合的方式进行粒度测量;通过增加采样次数,使测量数据更加准确可靠;由激光法与筛析-沉降法、图像分析法的比对可知,证明激光法检测碎屑岩粒度是可行的。     

A Process to Produce Effervescent Tablets: Fluidized Bed Dryer Melt Granulation

The purpose of the present study was to apply melt granulation in a fluidized bed dryer (fluidized bed dryer melt granulation) to manufacture one-step effervescent granules composed of anhydrous citric acid and sodium bicarbonate to make tablets. This study permitted us to establish that such process parameters as concentrations of polyethylene glycol (PEG) 6000, residence times in the fluidized bed dryer, fineness of PEG6000, fineness of initial mixture effervescent systems, and efficiency of two lubricants markedly affect some granule and tablet characteristics. It is a dry process that is simple, rapid, effective, economical, reproducible, and particularly adapted to produce effervescent granules that are easily compressed into effervescent tablets.     

Manufacture of Slow-Release Matrix Granules by Wet Granulation with an Aqueous Dispersion of Quaternary Poly(meth)acrylates in the Fluidized Bed

ABSTRACT

Slow-release matrix granules were manufactured in the fluidized bed using an aqueous dispersion of quaternary poly(meth)acrylates (Eudragit® RS 30 D) as binder for granulation. A factorial design was carried out to investigate the influence of the following parameters, spraying rate, applied polymer amount, and inlet air temperature, on various granule properties. Prerequisites for a slow release of the model drug theophylline are high spraying rate, high amount of polymer, and low inlet air temperature. No considerable decrease of the drug release rate can be achieved without a subsequent curing of the dry granules. A clear correlation exists between the moisture content of the fluidized bed, indicated by the terminal moisture content (TMC), and the mean dissolution time for 80% of the drug (MDT₈₀).     

大型循环流化床底部区域颗粒浓度分布研究

为获得内径400mm、高9100mm的大型循环流化床底部区域颗粒浓度分布规律,利用光导纤维探头研究了该区域颗粒浓度的径向分布。实验结果表明,颗粒浓度径向分布不均匀,呈现出典型的环-核结构。r/R=0.8可以作为环-核分界点。增大颗粒循环速率,颗粒浓度增大,边壁区域增大幅度比中心区域大。增大表观气速,颗粒浓度减小,边壁区域减小幅度比中心区域大。径向不同位置颗粒浓度随轴向高度增加均减小,边壁区域减小幅度比中心区域大。     

Using Experimental Design to Optimize the Process Parameters in Fluidized Bed Granulation

In this study many parameters were screened for a small-scale granulation process for their effect on the yield of granules between 75 and 500 μm and the geometrical granule mean size (d50). First a Plackett-Burman design was applied to screen the inlet air temperature, the inlet flow rate, the spray rate, the nozzle air pressure, the nozzle spray diameter, and the nozzle position. The Plackett-Burman design showed that the key process parameters were the inlet flow rate and the spray rate and probably also the inlet air temperature. Afterward a fractional factorial design (2^5?2) was applied to screen the remaining parameters plus the nozzle aircap position and the spraying time interval. The fractional factorial design showed that the nozzle air pressure was also important. As the target values for the granule yield (between 75 and 500 μm) and the geometric mean granule size (between 300 and 500 μm) were reached during the screening experiments, further optimization was not considered necessary.     

彩色负片的影像颗粒度

本文从卤化银颗粒、主成色剂分散及应用、以及DIR、DLAR成色剂的研究应用探讨改善彩色负片影像颗粒度的方法。     

Granulation in a Fluidized Bed II Effect of Binder Amount on the Final Granules

Abstract

There are many parameters affecting the properties of the final granules prepared in a fluidized bed. In this study one of the product parameters, quantity of the binder, has been studied for its effect on the final granule size, size distribution and friability

Determination of granule size change as a function of binder quantity leaded us to study the growth mechanisms during fluidized bed granulation. Two mechanisms are suggested;

1) Snowballing of primary granules (nuclei)

2) Agglomeration of primary granules

It has been shown that there is a critical amount of binder at which the formation of the primary granules comes to an end if more binder is added to the system. Then granule growth occurs by agglomeration of the primary granules. The physical properties of the granules formed before and after this critical binder concentration varies significantly     

Granulation in a Fluidized Bed II Effect of Binder Amount on the Final Granules

There are many parameters affecting the properties of the final granules prepared in a fluidized bed. In this study one of the product parameters, quantity of the binder, has been studied for its effect on the final granule size, size distribution and friability

Determination of granule size change as a function of binder quantity leaded us to study the growth mechanisms during fluidized bed granulation. Two mechanisms are suggested;

1) Snowballing of primary granules (nuclei)

2) Agglomeration of primary granules

It has been shown that there is a critical amount of binder at which the formation of the primary granules comes to an end if more binder is added to the system. Then granule growth occurs by agglomeration of the primary granules. The physical properties of the granules formed before and after this critical binder concentration varies significantly