Results 31 to 40 of about 2,280 (207)
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1989 A model was proposed to describe the expansion behavior of a gas fluidized bed of fine particles by using the elastic wave velocity. The difference between the maximum bed voidage in homogeneous fluidized beds, emb, and the emulsion-phase voidage in bubbling beds, ee could be explained by the proposed model.
Kai, Takami, Takahashi, Takeshige
openaire +2 more sources
Buoyancy Profile Inhibition of Turbulence in Nearly Vertical Bubbly Shear Flow
NUST Journal of Engineering Sciences, 2008 We report mea.sUICJD.CD.ts of two-dimensional (B/D::S) fully tw:bulent and developed duct flows (overall length/depth. IlD=60; D-based Reynolds number Re>104) for inclinations to 30 degrees from vertical at low voidagcs (
Khairuddin Sanaullah, N. H. Thomas
doaj +1 more source
Investigation into the hydrodynamics of liquid-solid inclined micro-fluidized beds
Resources Chemicals and Materials, 2022 The inclined micro-fluidized bed (MFB) can enhance heat and mass transfer rates compared to the vertically aligned counterparts, but the increased significance of surface forces and wall effects may cause poor fluidization performance. In this paper, the
Yi Zhang +4 more
doaj +1 more source
Chemical Engineering Journal Advances, 2021 The terminal settling velocity (TSV) of solid particles is experimentally determined in fluidizing columns. In monodispersed (single component) systems, the bed expansion behavior has been experimented with using pseudoplastic liquids.
Samit Bikas Maiti +2 more
doaj +1 more source
工程科学学报Ensuring full contact between hot sinters and cooling gas is the key premise for the widespread application of vertical sinter cooling technology at an industrial scale.
Yu ZHANG +3 more
doaj +1 more source
Effects of particle size and content of RDX on burning stability of RDX-based propellants
Defence Technology, 2022 Particle size and content of RDX are the two main factors that affect the burning stability of RDX-based propellants. However, these effects and the corresponding mechanisms are still controversial.
Bin-bin Wang +3 more
doaj +1 more source
KONA Powder and Particle Journal, 2018 Experimental data on the hydrodynamic behavior of dense and circulating fluidized beds at high temperatures are scarce in the literature. This work deals with the hydrodynamic study of a Fast Internally Circulating Fluidized Bed (FICFB) used for biomass ...
Sébastien Pecate +5 more
doaj +1 more source
Gas and solid behaviours during defluidisation of Geldart-A particles [PDF]
, 2011 Bed collapsing experiments were carried out in a cold-air transparent column 192 mm in diameter and 2 m high. Typical Fluid Catalytic Cracking (FCC) catalyst with a mean particle size of 76 μm and a density of 1400 kg/m3 was used.
E.T. Santos +7 more
core +1 more source
Integral Experiments and Magnetic Resonance Imaging of Lab‐Scale Liquid Distributors
Chemie Ingenieur Technik, EarlyView.Four lab‐scale liquid distributors were evaluated based on the homogeneity of the resulting liquid distribution. The best‐performing design reduced maldistribution and wall flow compared to a single‐point liquid distribution and remained stable under varying operating conditions, including different gas and liquid loads.
Hannah S. Rennebaum +4 more
wiley +1 more source
Chemie Ingenieur Technik, EarlyView.Combining the coating and transportation of particles into a single process step promises time savings and omits the need for separate coating equipment. Experiments were conducted using a vacuum pneumatic conveying system equipped with custom rapid‐prototyped nozzles and coating chambers.
G. van den Berg, J. A. Lindner
wiley +1 more source