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Liquid‐Solid mass transfer in a slurry bubble column and a gas‐liquid‐solid three‐phase fluidized bed
Author(s) -
Kikuchi KenIchi,
Takahashi Hiroshi,
Sugawara Takuo
Publication year - 1995
Publication title -
the canadian journal of chemical engineering
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.404
H-Index - 67
eISSN - 1939-019X
pISSN - 0008-4034
DOI - 10.1002/cjce.5450730307
Subject(s) - slurry , mass transfer , dissolution , dimensionless quantity , fluidized bed , bubble , particle (ecology) , ion exchange resin , materials science , inert , phase (matter) , superficial velocity , analytical chemistry (journal) , bead , particle size , chemistry , chromatography , thermodynamics , composite material , mechanics , inorganic chemistry , physics , oceanography , flow (mathematics) , organic chemistry , geology
Abstract Mass transfer coefficients between particles and liquids in a slurry bubble column and a three‐phase fluidized bed containing small size particles were obtained with two mass transfer systems: (1) K + –Na + ion‐exchange in cation‐exchange resin bead beds, including anion‐exchange resin beads as inert particles; (2) zinc dissolution by HCl in zinc‐plated glass bead beds, and in beds of non‐plated glass beads. Operating parameters were gas velocity, liquid velocity, particle diameter, and particle concentration. The dependence of mass transfer coefficients on these parameters is discussed from the viewpoint of the energy supplied into the systems. Correlations of the experimental data using dimensionless groups are compared to previous correlations.