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Powder Technology 1991: Vol 67 Index PDF

5 Pages·1991·0.82 MB·English
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Preview Powder Technology 1991: Vol 67 Index

Powder Technology, 67 (1991) 297 Author Index of Volume 67 Abanades, J. C., 113 Garboczi, E. J., 121 Lin, C. L., 103 Satoh, M., 11 Abu-Zaid, S., 1 Garcia, J. C., 291 Lum, L.-S. H., 201 Saxena, S. C., 265 Adanez, J., 113 Garnero, L., 27 Scarlett, B., 237, 249 Ahmadi, G., 1 Gautam, M., 187 Schneider, C. L., 103 Alonso, M., 11 Geldart, D., 163 McKenzie, Jr., E. A., 187 Shen, Z., 93 Artos, V., 291 Graf, J. C., 83 Malghan, S. G., 201 Sohoni, S., 277 Azzi, M., 27 Mandal, G., 277 Sridhar, R., 277 Haggblad, H.-A., 127 Mazza, G. D., 137 Srinivas, B. K., 15 Baeyens, J., 217 Higashi, K., 11 Miller, J. D., 103 Barreto, G. F., 137 Hongzhong Li, 37 Minor, D. B., 201 Thompson, L., 57 Beeckmans, J. M., 67 Miyanami, K., 11 Tory, C. B., 71 Bergougnou, M. A., 93 Ito, T., 11 Tory, E. M., 71 Bernard, J. R., 27 Turlier, P., 27 Berto, C. A., 137 Janczuk, B., 223 Nieh, S., 229 Bhatia, S. K., 145, 153 Jones, P., 163 van den Bergh, W. J. Bialopiotrowicz, T., 223 237, 249 Briens, C. L., 87, 93 Kamel, M. T., 71 Peleg, M., 21 Khakhar, D. V., 145, 153 Peri, S. S., 287 Wojcik, W., 22 Chhabra, R. P., 15, 287 King, R. P., 103 Pis, J. J., 291 Clark, N. N., 57, 187 Kwauk, M., 93 Popplewell, L. M., 21 Das Gupta, S., 145 Xuereb, C., 43 Laguérie, C., 43 de Lannoy, M. R. J., 249 Latkovic, D., 207 Rao, N. S., 265 Yousuf, M., 265 me FE. Fa ae Lee, S. W. 229 Rao, S. J., 153 Fuertes, A. B., 291 Levy, E. K., 207 Rubiera, F., 291 Zimmels, Y., 175 Elsevier Sequoia/Printed in The Netherlands Powder Technology, 67 (1991) 298-300 Subject Index of Volume 67 n-Alkane Electroconductivity coal film—air bubble—water systems and froth flota- regular electroconductive networks made from metal- tion of coal: stability of, 223 coated plastic powders: effect of plastic particle Attrition size on conductivity, 11 prediction of, in continuous fluid bed system, 291 Axial transport Filtration systems of granular solids in horizontal rotating cylinders: probabilistic design approach for, 175 experiments in non-flow system, 153 Fine grinding theory, 145 effect of grinding aids on, of limestone, quartz and Portland cement clinker, 277 Ball mill Fine particles high-energy agitation: silicon nitride powder milling importance of resolution limits to interpretation of kinetics in, 201 fractal descriptions of, 83 Binary powder mixtures Fine powders compressible: segregation of, subjected to tapping, 21 and viscous liquid; hydrodynamic and heat transfer Brittle particulate solids investigations conducted in bubble column with, influence of particle breakage on wall friction coeffi- 265 cient of: application to silo design, 249 Flow characteristics influence of wall inclination, normal load displace- of fluidized magnetite powder in inclined open chan- ment, 237 nel, 207 Bubble column Fluid bed hydrodynamic and heat transfer investigations con- circulating; mapping solid concentration in, using ducted in, with fine powders and viscous liquid, gammametry, 27 265 continuous, system; prediction of attrition in, 291 Bubble—water systems Fluid flow coal/n-alkane film—air, systems and froth flotation of non-Newtonian (purely viscous), through packed coal; stability of, 223 beds: effect of particle shape, 15 Fluidization velocities Circulating fluid bed minimum, of fluidized-bed coal-combustion solids, mapping solid concentration in, using gammametry, 113 27 Fluidization velocity Clusters minimum; effect of operating temperature on, 217 sedimentation of, of identical spheres: periodic mo- Fluidized bed tion of four spheres, 71 coal-combustion solids; minimum fluidization veloci- Coal ties of, 113 ‘n-alkane film—air bubble—water systems and froth effects of tube orientation and gas velocity on ero- flotation of coal: stability of, 223 sion of tube inserted into, 229 -combustion solids, fluidized-bed: minimum fluidiza- gas-; behaviour of continuous horizontal or inclined tion velocities of, 113 jets introduced into: morphology of jets, 43 Combustion slugging; differential pressure measurements in, minimum fluidization velocities of fluidized-bed coal- 187 combustion solid, 113 two-dimensional; jet presence probability in, 93 Compaction Fluidized magnetite powder segregation of compressible binary powder mixtures flow characteristics of, in inclined open channel, subjected to tapping, 21 207 Conductivity Fluid—particle flow regular electroconductivity networks made from phase diagram and ideal sealing state for vertical metal-coated plastic powders: effect of plastic moving bed, 37 particle size on conductivity, 11 Fractal descriptions Constitutive models importance of resolution limits to interpretation of, for powder materials, 127 of fine particles, 83 Free-fall velocity Dense particulate media simple method for estimation of, of spherical parti- evaluation of radiative heat transfer properties in, cles in power law liquids, 287 137 Froth flotation Differential pressure measurements of coal and stability of coal/n-alkane film—air in slugging fluidized bed, 187 bubble—water systems, 223 Elsevier Sequoia/Printed in The Netherlands Gammametry Packed beds mapping solid concentration in circulating fluid bed non-Newtonian (purely viscous) fluid flow through: using, 27 effect of particle shape, 15 Gas-fluidized bed Particle breakage behaviour of continuous horizontal or inclined jets influence of, on wall friction coefficient of brittle introduced into: morphology of jets, 43 particle solids: Gas velocity application to silo design, 249 and tube orientation; effects of, on erosion of tube influence of wall inclination, normal load dis- inserted into fluidized bed, 229 placement, 237 Granular powders Particle drag prediction behaviour of L-valves with, 163 holistic approach to, 57 Granular simple shear flows Particle shape analysis of, with rate-dependent model, 1 effect of; non-Newtonian (purely viscous) fluid flow Granular solids through packed beds, 15 axial transport of, in horizontal rotating cylinders: Particle size experiments in non-flow system, 153 plastic: effect of, on conductivity; regular electrocon- theory, 145 ductive networks made from metal-coated plastic Grinding aids powders, 11 effect of, on fine grinding of limestone, quartz and Periodic motion Portland cement clinker, 277 of four spheres; sedimentation of clusters of identi- cal spheres, 71 Heat transfer Permeability calculations and hydrodynamic investigations conducted in bubble mercury porosimetry and effective networks for, in column with fine powders and viscous liquid, 265 porous materials, 121 Holistic approach Phase diagram to particle drag prediction, 57 fluid—particle flow, and ideal sealing state for vertical Hydrodynamic investigations moving bed, 37 and heat transfer investigations conducted in bubble Plastic powders column with fine powders and viscous liquid, 265 regular electroconductivity networks made from metal-coated: effect of plastic particle size on Jet(s) conductivity, 11 Pneumatic transport line morphology of; behaviour of continuous horizontal solids volume fraction at injection point in, 67 or inclined jets introduced into gas-fluidized bed, 43 Porosimetry mercury, and effective networks for permeability cal- presence probability in two-dimensional fluidized culations in porous materials, 121 bed, 93 Portland cement clinker and limestone and quartz; effect of grinding aids on Limestone fine grinding of, 277 and quartz and Portland cement clinker; effect of Powder materials grinding aids on fine grinding of, 277 constitutive models for, 127 L-valves Power law fluids behaviour of, with granular powders, 163 Newtonian and pseudoplastic; correlation for direct calculation of terminal velocity of spherical parti- Magnetite powder cles in, 87 fluidized; flow characteristics of, in inclined open Power law liquids channel, 207 simple method for estimation of free-fall velocity of Mercury porosimetry spherical particles in, 287 and effective networks for permeability calculations Probabilistic design approach in porous materials, 121 for filtration systems, 175 Milling kinetics silicon nitride powder, in high-energy agitation ball mill, 201 Morphology Quartz of jets; behaviour of continuous horizontal or and limestone and Portland cement clinker; effect of inclined jets introduced into gas-fluidized bed, grinding aids on fine grinding of, 277 43 Newtonian and pseudoplastic fluids (power-law); correlation for direct calculation of ter- Radiative heat transfer properties minal velocity of spherical particles in, 87 evaluation of, in dense particulate media, 137 Random fracture model Operating temperature improved transformation technique for prediction of effect of, on minimum fluidization velocity, 217 liberation by, 103 300 Rotating cylinders Solids volume fraction axial transport of granular solids in horizontal: at injection point in pneumatic transport line, 67 experiments in non-flow system, 153 Spherical particles theory, 145 correlation for direct calculation of terminal velocity of, in Newtonian and pseudoplastic (power-law) fluids, 87 Sedimentation sedimentation of clusters of identical spheres: peri- of clusters of identical spheres: periodic motion of odic motion of four spheres, 71 four spheres, 71 simple method for estimation of free-fall velocity of, Segregation in power law liquids, 287 of compressible binary powder mixtures subjected to tapping, 21 Terminal velocity Shear flows correlation for direct calculation of, of spherical par- analysis of granular simple, with rate-dependent ticles in Newtonian and pseudoplastic (power- model, 1 law) fluids, 87 Silicon nitride powder milling kinetics in high-energy agitation ball mill, Wall friction coefficient 201 influence of particle breakage on, of brittle particu- Silo design late solids: application to; influence of particle breakage on wall application to silo design, 249 friction coefficient of brittle particulate solids, influence of wall inclination, normal load dis- 249 placement, 237 Erratum Powder Technology, 66 (1991) 265-280 The compaction behaviour of particulate materials. An elucidation based on percolation theory L. E. Holman (King of Prussia, PA, U.S.A.) Page 271, |.h. column, Fig. 3. This figure was unfortunately inverted prior to printing and should appear as follows: a oPobr = ar opaonyb se. Payy g p2o h q wos

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