Table Of Content

vi 3 ; ELSEVIER Powder Technology 100 (1998) 279 Author Index of Volume 100 Agrawal, K., 173 Isobe, T., 46 Naito, M., 52, 61 Tsubaki, J., 52 Ami, K., 46 Ito, S., 32 Nakahira, K., 52, 61 Tsutsumi, A., 237 Amirthaganesh, S.., Iwadate, Y., 223 Nakai, S., 15 Tuzla, K., 166 Awano, M., 74 Pan, X., 69 Bagyi, 1., 190 Jin, Y., 183 Parker, D.J., 242 van Baten, J.M., 137 Bergougnou, M.A., Jiyu, Z., 41 Pfeffer, R., 190 Van Den Akker, H.E.A., 123 Bijiang, Z., 41 Johnston, P.M., 260 van de Wall, R.E., 119 Brodkey, R.S., 161 Junichiro, T., 61 Qian, G., 76 Qian, G.-H., 190 Chaouki, J., 211 Kadambi, J.R., 251 Qingru, C., 80 Wang, Z., 183 Chen, J.C., 166 Kawamura, S., 32 Wei, F., 183 Cheng, Y., 183 Knowlton, T.M., 173 Reddy Karri, $.B., 173 Wen, L., 76 Choi, W.S., 78 Kousaka, Y., 7, 15 Saito, Y., 237 WWierrtnhe,t , K.ME..P,. ,1 6265 1 Deiva Venkatesh, R., 211 Krishna, R., 137 Schiewe, T., 166 Kuwahana, Y., 74 de Lasa, H.I., 260 Senna, M., 46 Kwauk, M., 3 Seville, J.P.K., 242 Yamazaki, R., 237 Ellenberger, J., 137 Sharma, A.K., 166 Yang, G., 103 Endo, Y., 15 Lee, D.J., 103 Shaw, H., 190 Yang, W.-C., 147 Epstein, N., 113 Li, C., 20 Shimizu, A., 24 Yaomin, Z., 80 Li, J., 76 Soo, S.L., 119 Yoshida, K., 237 Fan, L.-S., 103 Liandi, S., 79 Squires, A.M., 200 Youzhi, L., 41 Lin, H., 183 Srivastava, A., 173 Grace, J.R., 113 Luo, X., 103 Stein, M., 242 Grmela, M., 211 Stevens, J.G., 190 Zhang, H., 260 Gu, H., 20 Sun, G., 76 Zhang, J.-P., 113 Ma, Z., 69 Sundaresan, S., 173 Zhang, S., 69 Hayakawa, O., 52, 61 Maoming, F., 80 Suzuki, H., 237 Zhao, X., 20 Hong, J., 80 Martin, W.T., 251 Zhao, Y., 161 Horio, M Molerus, O., 166 Tanaka, T., 32 Zheng, B., 20 Mori, H., 52 Thomas, B., 200 Zhu, J.-X., 260 Elsevier Science S.A. ELSEVIER Powder Technology 100 (1998) 281-283 Subject Index of Volume 100 Aggiomerating fluidization Deagglomeration prediction of agglomerate sizes in bubbling fluidized beds of group C experimental analysis of sample preparation conditions for particle size powders, 223 measurement, 61 Agglomeration Defocus simulations of vibrated fine powders, 211 particle sizing using Particle Imaging Velocimetry for two-phase Anisotropy shape flows, 251 effect of particle shape on the particle size distribution measured with Diffraction commercial equipment, 52 particle sizing using Particle Imaging Velocimetry for two-phase Attrition flows, 251 attrition of porous glass particles in a fluidised bed, 242 Dispersion Averaging in multiphase flow a new sizing technique for fine powders dispersed in air, 15 a numerical validation of continuum time averaging, 119 Distributor separation of a binary particle mixture in a vibrating fluidized bed of Breakage behavior dense medium, 41 breakage behavior of quartz in a laboratory stirred bal! mill, 69 Downer Bubble columns transient dynamics of solid concentration in downer fluidized bed, 166 coherent structures in multiphase flows, 123 Dynamic simulation Bunkering phenomenon simulations of vibrated fine powders, 211 confirmation of Faraday’s explanation of bunkering in vibrated granular beds, 200 Faraday circulation confirmation of Faraday's explanation of bunkering in vibrated Calibration procedure granular beds, 200 a novel calibration procedure for a fiber optic solids concentration Fast fluidization probe, 260 transient dynamics of solid concentration in downer fluidized bed, 166 Capacitance tomography Fast fluidized bed dynamics of gas-particle flow in circulating fluidized beds, 173 multi-component granulation in a fast fluidized bed, 237 Ceramic filter FCC particles changes in pressure loss and face velocity of ceramic candle filters dynamics of gas-particle flow in circulating fluidized beds, 173 caused by reverse cleaning in hot coal gas filtration, 32 Fiber optic Circulating fluidized bed a novel calibration procedure for a fiber optic solids concentration dynamics of gas-particle flow in circulating fluidized beds, 173 probe, 260 profiles of particle velocity and solids fraction in a high-density riser, 183 Filtration changes in pressure loss and face velocity of ceramic candle filters Coal gasification caused by reverse cleaning in hot coal gas filtration, 32 changes in pressure loss and face velocity of ceramic candle filters caused by reverse cleaning in hot coal gas filtration, 32 Fine ceramic powder Coarse solids effect of particle shape on the particle size distribution measured with commercial equipment, 52 minimum fluidization velocities for gas—liquid-solid three-phase systems, 113 Flow structures Coherent motions coherent structures in multiphase flows, 123 coherent structures in multiphase flows, 123 Fluidised beds Cohesive particles attrition of porous glass particles in a fluidised bed, 242 prediction of agglomerate sizes in bubbling fluidized beds of group C Fluidization velocities powders, 223 minimum fluidization velocities for gas—liquid-solid three-phase Computational fluid dynamics systems, 113 scale effects in fluidized multiphase reactors, 137 Fluidized bed Concentration probe separation of a binary particle mixture in a vibrating fluidized bed of a novel calibration procedure for a fiber optic solids concentration dense medium, 41 probe, 260 comparison of jetting phenomena in 30-cm and 3-m diameter semi- Core shell composite particles circular fluidized beds, 147 physical and chemical interactions in multi-component composite Fluidized beds particles prepared by mechanical stressing, 46 coherent structures in multiphase flows, 123 Elsevier Science S.A. 282 Subject Index of Volume 100 /P owder Technology 100 (1998) 281-283 Gas-liquid—solid Particle morphology minimum fluidization velocities for gas—liquid—solid three-phase acetate-derived ZnO ultrafine particles synthesized by spray pyrolysis, systems, 113 20 Gas-solid fluidized bed Particle paths scale effects in fluidized multiphase reactors, 137 particle paths in three-dimensional flow fields as a means of study: Gas interchange Opposing jet mixing system, 161 comparison of jetting phenomena in 30-cm and 3-m diameter semi- Particle pressure circular fluidized beds, 147 prediction of agglomerate sizes in bubbling fluidized beds of group C Gas jets powders, 223 attrition of porous glass particles in a fluidised bed, 242 Particle science Granulation the history and recent activities of the Society of Powder Technology, multi-component granulation in a fast fluidized bed, 237 Japan, 7 Particle shape High density effect of particle shape on the particle size distribution measured with profiles of particle velocity and solids fraction in a high-density riser, commercial equipment, 52 183 Particle-size analyzer High pressure effect of particle shape on the particle size distribution measured with single bubble formation in high pressure liquid—solid suspensions, 103 commercial equipment, 52 Particle size distribution Instability suitability of the kinetic model for estimation of powder reaction rate, dynamics of gas-particle flow in circulating fluidized beds, 173 24 Intensity weighting Particle size measurement particle sizing using Particle Imaging Velocimetry for two-phase a new sizing technique for fine powders dispersed in air, 15 flows, 251 effect of particle shape on the particle size distribution measured with commercial equipment, 52 Jet mixing system experimental analysis of sample preparation conditions for particle size particle paths in three-dimensional flow fields as a means of study: measurement, 61 opposing jet mixing system, 161 Particle velocity Jets profiles of particle velocity and solids fraction in a high-density riser, comparison of jetting phenomena in 30-cm and 3-m diameter semi- 183 circular fluidized beds, 147 Phase locking coherent structures in multiphase flows, 123 Kinetic model PIV suitability of the kinetic model for estimation of powder reaction rate, particle sizing using Particle Imaging Velocimetry for two-phase 24 flows, 251 breakage behavior of quartz in a laboratory stirred ball mill, 69 Porous glass particles attrition of porous glass particles in a fluidised bed, 242 Laser Positron emission particle tracking (PEPT) particle sizing using Particle Imaging Velocimetry for two-phase attrition of porous glass particles in a fluidised bed, 242 flows, 251 Powder reaction rate Liquid—solid suspension suitability of the kinetic model for estimation of powder reaction rate, single bubble formation in high pressure liquid—solid suspensions 24 Powders Mechanochemistry simulations of vibrated fine powders, 211 physical and chemical interactions in multi-component composite Powder synthesis particles prepared by mechanical stressing, 46 MgTiO, acetate-derived ZnO ultrafine particles synthesized by spray pyrolysis, physical and chemical interactions in multi-component composite 20 particles prepared by mechanical stressing, 46 Powder technology Minimum fluidization velocity and distributor the history and recent activities of the Society of Powder Technology, a parametric study of a horizontal rotating fluidized bed using slotted Japan, 7 and sintered metal cylindrical gas distributors, 190 Pressure drop Mixed sample a parametric study of a horizontal rotating fluidized bed using slotted experimental analysis of sample preparation conditions for particle size and sintered metal cylindrical gas distributors, 190 measurement, 61 Pressure loss Monte Carlo simulation of gas-particle suspension changes in pressure loss and face velocity of ceramic candle filters a numerical validation of continuum time averaging, 119 caused by reverse cleaning in hot coal gas filtration, 32 Multi-component Primary particle multi-component granulation in a fast fluidized bed, 237 a new sizing technique for fine powders dispersed in air, 15 Pulse jet Non-oxide changes in pressure loss and face velocity of ceramic candle filters experimental analysis of sample preparation conditions for particle size caused by reverse cleaning in hot coal gas filtration, 32 measurement, 61 Particle aggregates Quartz grinding a new sizing technique for fine powders dispersed in air, 15 breakage behavior of quartz in a laboratory stirred ball mill, 69 Subject Index of Volume 100 / Powder Technology 100 (1998) 281-283 Random nucleation Solids fraction acetate-derived ZnO ultrafine particles synthesized by spray pyrolysis, profiles of particle velocity and solids fraction in a high-density riser, 20 183 Rotating fluidized bed Spray pyrolysis a parametric study of a horizontal rotating fluidized bed using slotted acetate-derived ZnO ultrafine particles synthesized by spray pyrolysis, and sintered metal cylindrical gas distributors, 190 20 Round robin Standpipe flow effect of particle shape on the particle size distribution measured with dynamics of gas-particle flow in circulating fluidized beds, 173 commercial equipment, 52 Stirred ball mill breakage behavior of quartz in a laboratory stirred ball mill, 69 Sample preparation conditions experimental analysis of sample preparation conditions for particle size Thermal decomposition measurement, 61 acetate-derived ZnO ultrafine particles synthesized by spray pyrolysis, Scale up 20 scale effects in fluidized multiphase reactors, 137 Three-dimensional flow fields Separation particle paths in three-dimensional flow fields as a means of study: separation of a binary particle mixture in a vibrating fluidized bed of opposing jet mixing system, 161 dense medium, 41 Two-phase model Single bubble formation scale effects in fluidized multiphase reactors, 137 single bubble formation in high pressure liquid—solid suspensions, 103 Size prediction van der Waals force prediction of agglomerate sizes in bubbling fluidized beds of group C prediction of agglomerate sizes in bubbling fluidized beds of group C powders, 223 powders, 223 Vibrated beds Sizing particle sizing using Particle Imaging Velocimetry for two-phase simulations of vibrated fine powders, 211 flows, 251 Vibrated granular bed Slurry reactors confirmation of Faraday’s explanation of bunkering in vibrated scale effects in fluidized multiphase reactors, 137 granular beds, 200 Society of Powder Technology Vorticity the history and recent activities of the Society of Powder Technology, coherent structures in multiphase flows, 123 Japan, 7 Solid concentration Zinc oxide transient dynamics of solid concentration in downer fluidized bed, acetate-derived ZnO ultrafine particles synthesized by spray pyrolysis, 166 20