1 - 12 |
Effects of operating factors on the particle size distribution and particle shape of synthesized precipitated CaCO3: effect of reaction temperature, blowing rate of CO2 gas and initial slurry concentration of Ca(OH)(2) on reaction completion time Park SY, Choi WS |
13 - 29 |
Computational model for prediction of particle degradation during dilute-phase pneumatic conveying: the use of a laboratory-scale degradation tester for the determination of degradation propensity Chapelle P, Abou-Chakra H, Christakis N, Patel M, Abu-Nahar A, Tuzun U, Cross M |
31 - 49 |
Computational model for prediction of particle degradation during dilute-phase pneumatic conveying: modeling of dilute-phase pneumatic conveying Chapelle P, Christakis N, Abou-Chakra H, Bridle I, Bradley MSA, Patel M, Cross M |
51 - 61 |
A feasibility study of a new photosynthesis bioreactor design using TiO2 particles combined with enzymes Kurayama F, Matsuyama T, Yamamoto H |
63 - 77 |
Three-dimensional particle shape descriptors for computer simulation of non-spherical particulate assemblies Abou-Chakra H, Baxter J, Tuzun U |
79 - 96 |
Statistical and power spectral analysis of quality of fluidization for different particle size distributions at high temperature Lin CL, Wey MY |
97 - 107 |
Mransparent observation of particle dispersion in alumina slurry using in situ solidification Takahashi M, Oya M, Fuji M |
109 - 129 |
Accurate wet-type centrifugal classification using an almost rigidly rotating flow - classification principle and performance of the batch-type classification Nakabayashi K, Tsuchida Y |
133 - 133 |
Activity of technical groups in APPIE: Battery manufacturing technology group Kohama H |