ISSN:
0006-3592
Keywords:
expanded bed adsorption
;
fluidization
;
viscosity
;
annexin V
;
Chemistry
;
Biochemistry and Biotechnology
Source:
Wiley InterScience Backfile Collection 1832-2000
Topics:
Biology
,
Process Engineering, Biotechnology, Nutrition Technology
Notes:
Expanded bed adsorption is a new downstream processing technique forcapture of proteins directly from unclarified feedstocks. Expanded bed adsorption reduces the number of operations in purification processes by combining clarification, concentration, and capture into one operation. It is based on stable fluidization and uses adsorbent particles with well-defined size and density distributions, together with columns designed to giveeven liquid flow distribution. The bed expands as the adsorbent particles are lifted by an upward liquid flow through the column. The behavior of the expanded bed is similar to a packed chromatography bed due to very little back-mixing of the adsorbent particles. The major benefit of using anexpanded bed is that adsorption can be carried out with unclarified feedstocks; there is no need for centrifugation or filtration to remove cells and debris. When the feedstock is applied, the target protein is captured by the adsorbent while cells and debris pass through the column unhindered. Washing is performed with the bed in an expanded mode, followed by elution of bound protein in a sedimented mode with downward flowDescribed in this article is the use of expanded bed adsorption for pilot scale recovery of recombinant human placental annexin V from an Escherichia coli ho mogenate. The description includes the whole procedure, from small-scale method optimization to pilot scale. The recovery of annexin V was approximately 95% at both lab scale and pilot scale. During the trials, it was discovered that the expanded bed was affected by the biomass content and viscosity of the homogenate. The upper limits for these parameters were therefore investigated further. For the E. coli used in the application described here, homogenates with biomass dry weightup to 5% and viscosities up to 10 mPa s (at a shear rate of 1 s-1) worked best. It was, however, feasible to use homogenates with dry weight up to 7-8% and viscosities up to 50 mPa s (1 s-1). © 1994 John Wiley & Sons, Inc.
Additional Material:
4 Ill.
Type of Medium:
Electronic Resource
URL:
http://dx.doi.org/10.1002/bit.260440808
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