Table Of Content

Powder Technology, 68 (1991) 293 Alonso, M., 145 Garic, R. V., 199 Luerkens, D. W., 163 Rajendran Nair, P. B., 79 Andersson, S., 117 Geoffroy, J. M., 91 Lyckowski, R. W., 37 Ramanujam, M., 79 Gidaspow, D., 13 Renz, U., 271 Bagchi, A., 85 Grbaveic, Z. B., 199 Maeder, A. J., 137 Beddow, J. K., 163 Satoh, M., 145 Matsumoto, T., 131 Berkelmann, K.-G., 271 Hadzismajlovic, Dz. E., 199 Smith, D. M., 53, 63, 71 Menéndez, M., 31 Bertrand, J., 213 He, Q. L., 187 Snyder, T. R., 159 Mianowski, A., 101 Bilbao, R., 31 Hidaka, N., 131 Miyanami, K., 145 Standish, N., 175, 187 Bilinski, B., 125 Hosoda, K., 1 Morgan III, M. H., 199 Bouillard, J. X., 13, 37 Hotta, N., 153 Takenouchi, H., 131 Morooka, S., 131 Bousquet, J., 213 Tanaka, M., 153 Bridoux, D., 213 Izquierdo, M. T., 31 Tanaka, T., 1 Briens, C. L., 243, 255 Niwano, J., 153 Thoma, S. G., 53, 63, 71 Burru, I. G., 243, 255 Johnsson, F., 117 Nomura, S., 1 Jovanovic, S., 199 Normand, M. D., 281 Venkata Ramayya, A., 287 Carstensen, J. T., 91 Nussinovitch, A., 281 Venkateshan, S. P., 287 Chhabra, R. P., 85 Kimura, I., 153 Vukovic, D. V., 199 Ciftcioglu, M., 53, 63, 71 Kolar, A. K., 287 Orr, N. A., 195 Clark, N. N., 137 Kozanoglu, B., 285 Waldie, B., 109 Orumwense, O. A., 23 Clift, R., 291 Wasilewski, P., 101 Leckner, B., 117 Wilkinson, D., 109 Egermann, H., 195 Levy, E. K., 285 Peleg, M., 281 Lezaun, J., 31 Peukert, W., 263 Yu, A. B., 175, 187 Fayolle, P., 213 Lin, I. J., 235 Polanski, J., 101 Forssberg, E., 23 Littman H., 199 Pontius, D. H., 159 Zhen Fan, 290 Fujita, T., 235 Léffler, F., 263 Poux, M., 213 Zou, R. P., 175 Elsevier Sequoia, Lausanne Powder Technology, 68 (1991) 295-296 Subject Index of Volume 68 Accelerating motion Fluid energy grinding of spherical particles in power law type non-Newtonian classification function in, 79 liquids, 85 Fluidized bed(s) Adipic acid “The analysis of pressure fluctuations in a 2-D fluidized effects of powder production and of material processing on bed”: powder particle morphology of, 163 comments on, 287 Agglomerate strength distributions editor’s closure on, 291 determination of: response to comments on, 290 application to model agglomerates, 63 combustor; gas and solid flow in freeboard of, 271 application to titania processing, 71 combustors; erosion of heat exchanger tube banks in, 37 calibration via ultrasonic forces, 53 floating-type, CVD; synthesis of AIN/SiC composite pow- Aggregates ders by, 153 uncompacted dust; measurement of tensile strength of, 159 freely bubbling; expansion of, 117 Agitated systems gas; wake fractions of small bubbles in, 285 some practical rules applied to: powder mixing, 213 segregation of straw/sand mixtures in, in non-steady state, AIN/SiC composite powders 31 synthesis of, by floating-type fluidized-bed CVD, 153 three-phase; particle—liquid mass transfer in: Newtonian liquids, 243 Barium titanate particles non-Newtonian liquids, 255 ultrafine; dielectric fluid preparation by dispersing, in variational model for prediction of fluid—particle interphase kerosene, 235 drag coefficient and particulate expansion of fluidized Basalt wastes and sedimenting beds, 199 briquetting of, 101 Fluid-particle interphase drag coefficient Briquetting and particulate expansion of fluidized and sedimenting of basalt wastes, 101 beds; variational model for prediction of, 199 Bubbles expansion of freely bubbling fluidized bed, 117 Galena origin of, and Geldart’s classification, 13 properties of hydration layers on surface of, precoated segregation of solid particles of two sizes in bubble with potassium ethyl xanthate, 125 columns, 131 Gas fluidized beds small: wake fractions of, in gas fluidized beds, 285 wake fractions of small bubbles in, 285 Bulk density Gas and solid flow maximum; optimization of coal grind for, 175 in freeboard of fluidized bed combustor, 217 Geldart’s classification origin of bubbles and, 13 Coal grind optimization of, for maximum bulk density, 175 Granular bed filters influence of temperature on particle separation in, 263 Coal heap Grinding experimental study of packing of, 187 fluid energy; classification function in, 79 Combustor(s) media; analysis of selection function for mills using balls fluidized bed: as, 1 erosion of heat exchanger tube banks in, 37 gas and solid flow in freeboard of, 271 Harmonic endurance new shape descriptor derived from polygonal harmonics, Density ratio 137 and size ratio and concentration; optimum combination of, Heat exchanger tube banks to minimize free surface segregation, 145 erosion of, in fluidized-bed combustors, 37 Dielectric fluid preparation Hydration layers by dispersing ultrafine barium titanate particles in properties of, on surface of galena precoated with potas- kerosene, 235 sium ethyl xanthate, 125 Drag coefficient variational model for prediction of fluid—particle interphase Kerosene drag coefficient and particulate expansion of fluidized dielectric fluid preparation by dispersing ultrafine barium and sedimenting beds, 199 titanate particles in, 235 Erosion Material processing of heat exchanger tube banks in fluidized-bed combustors, and power production; effects of, on powder particle mor- 37 phology of adipic acid, 163 Elsevier Sequoia, Lausanne 296 Measurement methods Segregation effects of, on properties of materials, 91 free surface; optimum combination of size ratio, density Mills ratio and concentration to minimize, 145 analysis of selection function for, using balls as grinding of solid particles of two sizes in bubble columns, 131 media, |] of straw/sand mixtures in fluidized beds in non-steady Mixed particle populations state, 31 theoretical, with unimodal size distribution, 281 Selection function Model analysis of, for mills using balls as grinding media, 1 agglomerates: application to; determination of agglomerate Silicon strength distributions, 63 synthesis of AIN/SiC composite powders by floating-type variational, for prediction of fluid—particle interphase drag fluidized-bed CVD, 153 coefficient and particulate expansion of fluidized and Size ratio sedimenting beds, 199 and density ratio and concentration; optimum combination Morphology of, to minimize free surface segregation, 145 powder particle; effects of powder production and of ma- Solid and gas flow terial processing on, of adipic acid, 163 in freeboard of fluidized bed combustor, 271 Solid particles Newtonian liquids segregation of, of two sizes in bubble columns, 131 particle—liquid mass transfer in three-phase fluidized beds, Solid mixing 243 comments on paper “Recent developments in solids mixing” by L. T. Fan ef al., 195 Spectral extinction Packing characterization of particle suspensions by: numerical experimental study of, of coal heap, 187 study, 109 Particle-liquid mass transfer Spherical particles in three-phase fluidized beds: accelerating motion of, in power law type non-Newtonian Newtonian liquids, 243 liquids, 85 non-Newtonian liquids, 255 Straw/sand mixtures Particle separation segregation of, in fluidized beds in non-steady state, 31 influence of temperature on, in granular bed filters, 263 Structural changes Particle suspensions and surface changes in wet ground minerals, 23 characterization of, by spectral extinction: numerical study, Surface 109 optimum combination of size ratio, density ratio and con- Particulate expansion centration to minimize free surface segregation, 145 of fluidized and sedimenting beds and fluid—particle inter- properties of hydration layers on, of galena precoated with phase drag coefficient; variational mode] for prediction potassium ethyl xanthate, 125 of, 199 and structural changes in wet ground minerals, 23 Potassium ethyl xanthate Synthesis properties of hydration layers on surface of galena pre- of AIN/SiC composite powders by floating-type fluidized- coated with, 125 bed CVD, 153 Powder mixing some practical rules applied to agitated systems, 213 Temperature influence Powder production on particle separation in granular bed filters, 263 and material processing; effects of, on powder particle Tensile strength morphology of adipic acid, 163 measurement of, of uncompacted dust aggregates, 159 Power law type non-Newtonian fluids Theoretical mixed particle populations accelerating motion of spherical particles in, 85 with unimodal size distribution, 281 Pressure fluctuations Titania processing “The analysis of pressure fluctuations in a 2-D fluidized application to: determination of agglomerate strength dis- bed”: tributions, 71 comments on, 287 editor’s closure on, 291 Ultrasonic forces response to comments on, 290 calibration via; determination of agglomerate strength distributions, 53 Unimodal size distribution Sand/straw mixtures theoretical mixed particle populations with, 281 segregation of, in fluidized beds in non-steady state, 31 Sedimenting beds Wake fractions variational model for prediction of fluid—particle interphase of small bubbles in gas fluidized beds, 285 drag coefficient and particulate expansion of fluidized Wet ground minerals and, 199 surface and structural changes in, 23