Literature DB >> 10397887

The influence of complex biological feedstock on the fluidization and bed stability in expanded bed adsorption

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Abstract

The stability of expanded bed adsorption systems (EBA) was studied in biomass containing culture broth by residence time distribution (RTD) experiments, using pulse inputs of fluorescent molecules as tracers. Different commercial adsorbents (Streamline DEAE, SP, Phenyl, Chelating, and AC) were tested at various biomass concentrations (2.5-12 %, wet weight) of whole (Saccharomyces cerevisiae) yeast, yeast cell homogenate, and Escherichia coli homogenate. Analyzing the RTD according to the PDE model (PDE: axially dispersed plug-flow exchanging mass with stagnant zones) allowed the calculation of three parameters: the number of transfer units for mass exchange between mobile and stagnant fraction (N), the Peclet number for overall axial dispersion (P), and the mobile fraction of the liquid in axially dispersed plug flow (varphi). When fluidization was performed in particle-free buffer the normalized response signal (after perfect input pulse) was symmetric (N:0; P: 50-100; varphi: 1), thus, demonstrating the formation of a homogeneous fluidized (expanded) bed. Upon application of suspended biomass the RTD was skewed, depending on the adsorbent used and the type and level of biomass present in the sample. This situation leads to three different characteristic pictures: the well-fluidized system (N: >/= 7-10; P: >/= 40; varphi: 0.80-0.90), the system exhibiting bottom channeling (N: < 1-2; P: >/= 40; varphi: 0.5-0.7) and, the system where extensive agglomeration develops (N: 4-7; P: 20-40; varphi: < 0.5). These results demonstrate that changes in the hydrodynamics of EBA already take place in the presence of moderate concentrations of biomass. Furthermore, those changes can be quantitatively described mainly in terms of the fraction of stagnant zones in the system, which are formed due to the interaction of biomass and adsorbent. The technique described here can be used to evaluate a certain combination of adsorbent and biomass with regard to its suitability for expanded bed adsorption from whole broth. Copyright 1999 John Wiley & Sons, Inc. Biotechol Bioeng 64: 484-496, 1999.

Entities:  

Year:  1999        PMID: 10397887     DOI: 10.1002/(sici)1097-0290(19990820)64:4<484::aid-bit11>3.0.co;2-z

Source DB:  PubMed          Journal:  Biotechnol Bioeng        ISSN: 0006-3592            Impact factor:   4.530


  2 in total

1.  Purification of recombinant nucleocapsid protein of Newcastle disease virus from unclarified feedstock using expanded bed adsorption chromatography.

Authors:  Yan Peng Tan; Tau Chuan Ling; Wen Siang Tan; Khatijah Yusoff; Beng Ti Tey
Journal:  Protein Expr Purif       Date:  2005-07-27       Impact factor: 1.650

2.  Mathematical modelling of expanded bed adsorption - a perspective on in silico process design.

Authors:  Victor Koppejan; Guilherme Ferreira; Dong-Qiang Lin; Marcel Ottens
Journal:  J Chem Technol Biotechnol       Date:  2018-04-06       Impact factor: 3.174

  2 in total

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