Chemical and Biomolecular Engineering Research and Publications
Date of this Version
6-13-2004
Abstract
This paper provides an approach for optimizing the cell density (Xc) and dilution rate (D) in a chemostat for a Pichia pastoris continuous fermentation for the extracellular production of a recombinant protein, interferon τ (INF-τ). The objective was to maximize the volumetric productivity (Q, mg INF-τ I-1 h-1), which was accomplished using response surface methodology (RSM) to model the response of Q as a function of Xc and D within the ranges 150 ≤ Xc ≤ 450 g cells (wet weight) l-1 and 0.1 μm ≤D ≤ 0.9 μm (μm =0.0678 h-1, the maximum specific growth rate obtained from a fed-batch phase controlled with a methanol sensor). The methanol and medium feed rates that resulted in the desired Xc and D were determined based on the mass balance. From the RSM model, the optimal Xc and D were 328.9 g h-1and 0.0333 h-1 for a maximum Q of 2.73 mg I-1 h-1. The model of specific production rate (q, mgINF- τ g-1 cells h-1) was also established and showed the optimal Xc=287.7 g I-1 and D=0.0361 h-1 for the maximum ρ(predicted to be 8.92•10-3 mg-3 g-1 h-1). The methanol specific consumption rate (v, g methanol g-1 cells h-1) was calculated and shown to be independent of the cell density. The relationship between v and μ (specific growth rate) was the same as that discovered from fed-batch fermentations of the same strain. The approach developed in this study is expected to be applicable to the optimization of continuous fermentations by other microorganisms.
Comments
This paper was published online: 15 July 2004 ©Society for Industrial Microbiology 2004