A systematic approach for the design of a bioproduct recovery process employing magnetic supports and the technique of high-gradient magnetic fishing (HGMF) is described. The approach is illustrated for the separation of superoxide dismutase (SOD), an antioxidant protein present in low concentrations (ca. 0.15-0.6 mg L(-1)) in whey. The first part of the process design consisted of ligand screening in which metal chelate supports charged with copper(II) ions were found to be the most suitable. The second stage involved systematic and sequential optimization of conditions for the following steps: product adsorption, support washing, and product elution. Next, the capacity of a novel high-gradient magnetic separator (designed for biotechnological applications) for trapping and holding magnetic supports was determined. Finally, all of the above elements were assembled to deliver a HGMF process for the isolation of SOD from crude sweet whey, which consisted of (i) binding SOD using Cu2+ -charged magnetic metal chelator particles in a batch reactor with whey; (ii) recovery of the "SOD-loaded" supports by high-gradient magnetic separation (HGMS); (iii) washing out loosely bound and entrained proteins and solids; (iv) elution of the target protein; and (v) recovery of the eluted supports from the HGMF rig. Efficient recovery of SOD was demonstrated at approximately 50-fold increased scale (cf magnetic rack studies) in three separate HGMF experiments, and in the best of these (run 3) an SOD yield of >85% and purification factor of approximately 21 were obtained.

The role of the proteins encoded by the GAL80 gene, the MIG1 gene and the GAL6 gene in glucose control of galactose consumption by Saccharomyces cerevisiae was studied by physiological characterisation of various GAL mutant strains. Dynamic experiments with the CEN.PK 113-7D wild-type strain and a deltagal80deltamig1 double-mutant strain in aerobic nitrogen-limited continuous cultivations at a dilution rate of 0.1 h(-1), showed simultaneous glucose and galactose consumption by the deltagal80deltamig1 strain. The wild-type strain did not consume galactose in the presence of glucose. Aerobic batch cultivations on glucose-galactose mixtures with the wild-type strain and with recombinant strains with a de-regulated GAL system (the deltagal80deltamig1 strain, a deltagal6 deleted strain, a deltagal6deltagal80deltamig1 triple mutant, and a deltagal6deltagal80deltamig1 triple mutant harbouring a GAL4 high-copy vector) were carried out. Generally, a reduction of glucose control lowered the maximum specific growth rate on glucose and increased the ethanol yield obtained on galactose with more than 100%. In contrast to the wild-type strain, the deltagal6deltagal80deltamig1 triple mutant strain consumed glucose and galactose simultaneously, and this strain also showed the highest ethanol production with an overall ethanol yield of 0.35 g g-1 sugar, which is 17% higher than the yield on glucose obtained with the wild-type strain. GAL80 and MIG1 were demonstrated to be responsible for the majority of the glucose control on the GAL system, whereas GAL6 has a minor role in glucose control. Deletion of GAL6 was shown to have a major impact on biomass and ethanol formation when cells were grown on galactose, and from the data obtained we speculate that Gal6 may be involved in mRNA degradation of the GAL gene transcripts.

BACKGROUNDThe extraction of biopharmaceuticals from plasma and serum often employs overly complicated antiquated procedures that can inflict serious damage on especially prone protein targets and which afford low purification power and overall yields. This paper describes systematic development of a high‐gradient magnetic fishing process for recovery of immunoglobulins from unclarified antiserum.RESULTSNon‐porous superparamagnetic particles were transformed into hydrophobic‐charge induction adsorbents and then used to recover immunoglobulins from rabbit antiserum feedstocks. Comprehensive characterisation tests conducted with variously diluted clarified antiserum on a magnetic rack revealed that immunoglobulin binding was rapid (equilibrium reached in <45 s), strong (Kd < 0.1 mg mL‐1), of high capacity (Qmax = 214 mg g‐1), and pH and ionic strength dependent. In a high‐gradient magnetic fishing process conducted with the same adsorbent, and a conventional ‘magnetic filter + recycle loop’ arrangement, >72% of the immunoglobulin present in an unclarified antiserum feed was recovered in 0.5 h in >3‐fold purified form.CONCLUSIONSFast magnetic particle based capture of antibodies from an unclarified high‐titre feed has been demonstrated. Efficient product recovery from ultra‐high titre bioprocess liquors by high‐gradient magnetic fishing requires that improved magnetic adsorbents displaying high selectivity, ultra‐high capacity and operational robustness are used with ‘state‐of‐the‐art’ rotor–stator magnetic separators. © 2018 The Authors. Journal of Chemical Technology & Biotechnology published by John Wiley & Sons Ltd on behalf of Society of Chemical Industry.

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