Pilot-scale harvest of recombinant yeast employing microfiltration: a case study

• Published in: Journal of biotechnology Vol. 42; no. 3; pp. 235 - 246
• Main Authors: Russotti, Gregory, Osawa, A.Edward, Sitrin, Robert D., Buckland, Barry C., Adams, William R., Lee, Steven S.
• Format: Journal Article
• Language: English
• Published: Lausanne Elsevier B.V 16-10-1995; Amsterdam Elsevier; New York, NY
• Subjects: Biological and medical sciences; Biotechnology; Crossflow filtration; Culture Media; Fermentation; Fundamental and applied biological sciences. Psychology; Methods. Procedures. Technologies; Microfiltration; Others; Recombinant; Recombination, Genetic; Saccharomyces cerevisiae; Saccharomyces cerevisiae - genetics; Saccharomyces cerevisiae - isolation & purification; Ultrafiltration; Various methods and equipments; Yeast; Microfiltration; Yeast; Crossflow filtration; Saccharomyces cerevisiae; Recombinant; Performance evaluation; Recombinant microorganism; Operating conditions; Pilot plant scale; Fungi; Biofouling; Membrane; Ascomycetes; Operating process; Thallophyta
• ISSN: 0168-1656; 1873-4863
• DOI: 10.1016/0168-1656(95)00083-3

In order to develop a cost-effective recovery process for an intracellular product, crossflow microfiltration was studied for the harvest of a recombinant yeast under severe time constraint. It was required to process yeast broth in a short period of time to minimize the risk for product degradation. Preliminary microfiltration studies employing flat sheet membranes showed high throughout with initial fluxes on the order of water fluxes (> 1000 LMH, regime I,
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), followed by a rapid decay towards a low pseudo-steady state flux (20 LMH, regime II, > 2 min). Exploitation of these high fluxes and control of their eventual decline were crucial in establishing a rapid crossflow filtration process. The effect of several parameters, such as initial cell concentration, shear rate, transmembrane pressure, membrane pore size and medium composition on filtration performance were investigated to better understand the flux decline mechanisms. We found that the major contributor to flux decay was reversible fouling by the cake formation on the membrane surface. Within the operating boundaries of our microfiltration system, large-pore membrane (0.65 μm) was much more desirable for harvesting our yeast (10 μ size) without cell leakage than smaller pore ones (0.22 μm and 0.45 μm). Among adjustable operating parameters, feed flow rate (i.e., shear rate) exerted significant impact on average flux, whereas manipulation of transmembrane pressure afforded little improvement. Although initial cell concentration affected adversely the permeation rates, growth medium components, especially soy-peptone, was deemed pivotal in determining the characteristics of cell cake, thus controlling yeast microfiltration.