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Experimental measurement of particle size distribution and voidage in an expanded bed adsorption system
Author(s) -
Willoughby N. A.,
Hjorth R.,
TitchenerHooker N. J.
Publication year - 2000
Publication title -
biotechnology and bioengineering
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 1.136
H-Index - 189
eISSN - 1097-0290
pISSN - 0006-3592
DOI - 10.1002/1097-0290(20000920)69:6<648::aid-bit9>3.0.co;2-u
Subject(s) - particle size , packed bed , mechanics , volumetric flow rate , residence time distribution , tracer , particle (ecology) , particle size distribution , constant (computer programming) , chemistry , chromatography , materials science , flow (mathematics) , geology , physics , oceanography , computer science , nuclear physics , programming language
This paper presents an experimental analysis of matrix bead size distribution and voidage variations with axial height in an expanded bed adsorption system. Use of a specially constructed expanded bed with side ports has enabled sampling from within the expanded bed along the vertical axis. Particles removed from within the bed were measured for their size distributions. Residence time distribution studies were used to estimate bed voidage. Measurements of axial and radial particle size distributions and axial voidage distribution have been made at different flow rates. Particle size was found to be radially constant, indicating constant stratification in the column. The particle size was found to decrease with increasing axial height. Voidage increased with axial height from a settled bed value of 0.39 to approaching unity for high liquid velocities and increased at a constant axial position with increased flowrate. This information provides key insight into bed stability and data for the improved modeling of this important unit operation. © 2000 John Wiley & Sons, Inc. Biotechnol Bioeng 69: 648–653, 2000.