Mean particle diameters. Part IV: Empirical selection of the proper type of mean particle diameter describing a product or material property

被引:17
作者
Alderliesten, M [1 ]
机构
[1] Unilever Res Labs, NL-3133 AT Vlaardingen, Netherlands
关键词
dispersed phase; granulation; mean diameter; moment-ratio; particle; size distribution;
D O I
10.1002/ppsc.200400917
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Mean particle diameters may be used to describe and to model physical, chemical or physiological properties of products or materials containing dispersed phases. An empirical method was developed to select the proper type of mean diameter from experimental data, if this mean diameter is not known a priori from theoretical reasoning. The present method uses mean diameters, (D) over bar (p, q), defined according to the Moment-Ratio (M-R) definition system. They are expressed as the 1/(p-q)-th power of the ratio of the p-th and the q-th raw moment of the number density distribution of the particle sizes. After calculation of the mean diameters, (D) over bar (p, q), the relationships between the product property and these mean diameters are investigated statistically. The selection method has been illustrated by four examples, three of which stem from a high shear granulation experiment in the field of detergent processing. The fourth example is concerned with a visual ranking of bubble size distributions of chocolate mousse samples. The data set of each example consists of a set of particle size distributions and the corresponding physical product properties that are influenced by the particle sizes. Hypotheses are formulated to explain the types of selected mean diameters. Application of the selection method gives mean diameters, (D) over bar (p, q), a clear physical look and identity, replacing their anonymity. Sharing worldwide results of applications of the newly developed selection method, will lead to a build-up of knowledge of physical meanings and application areas for the types of the mean particle diameters. This will support decision-making in product development. The examples used to develop the selection method clearly demonstrate the physical relevance of the previously developed nomenclature system for mean particle diameters, (D) over bar (p, q).
引用
收藏
页码:179 / 196
页数:18
相关论文
共 24 条
[1]   Mean particle diameters. part III: An empirical evaluation of integration and summation methods for estimating mean particle diameters from histogram data [J].
Alderliesten, M .
PARTICLE & PARTICLE SYSTEMS CHARACTERIZATION, 2002, 19 (06) :373-386
[2]   MEAN PARTICLE DIAMETERS .2. STANDARDIZATION OF NOMENCLATURE [J].
ALDERLIESTEN, M .
PARTICLE & PARTICLE SYSTEMS CHARACTERIZATION, 1991, 8 (03) :237-241
[3]   MEAN PARTICLE DIAMETERS .1. EVALUATION OF DEFINITION SYSTEMS [J].
ALDERLIESTEN, M .
PARTICLE & PARTICLE SYSTEMS CHARACTERIZATION, 1990, 7 (04) :233-241
[4]  
BAIRD JC, 1978, FUNDAMENTALS SCALING, P17
[5]  
Campbell MR, 1996, CEREAL CHEM, V73, P536
[6]   Effect of particle size, air flow and inhaler device on the aerosolisation of disodium cromoglycate powders [J].
Chew, NYK ;
Bagster, DF ;
Chan, HK .
INTERNATIONAL JOURNAL OF PHARMACEUTICS, 2000, 206 (1-2) :75-83
[7]  
DAVIES OL, 1972, STAT METHODS RES PRO, P29
[8]   A MICROLEVEL-BASED CHARACTERIZATION OF GRANULATION PHENOMENA [J].
ENNIS, BJ ;
TARDOS, G ;
PFEFFER, R .
POWDER TECHNOLOGY, 1991, 65 (1-3) :257-272
[9]  
HERDAN G, 1960, SMALL PARTICLE STAT, pCH4
[10]   Nucleation, growth and breakage phenomena in agitated wet granulation processes: a review [J].
Iveson, SM ;
Litster, JD ;
Hapgood, K ;
Ennis, BJ .
POWDER TECHNOLOGY, 2001, 117 (1-2) :3-39