Scale-up of recombinant cutinase recovery by whole broth extraction with PEG-phosphate aqueous two-phase

A whole broth extraction using an aqueous two-phase system (ATPS) composed by 5% (w/w) PEG 3350 and 15% (w/w) phosphate was used for the scale-up extraction and isolation of a recombinant Fusarium solani pisi cutinase, an extracellular mutant enzyme expressed in Saccharomyces cerevisiae, containing a fusion peptide (WP)4. The experiments were carried out at three different scales (10 ml, 1 l and 30 l). Mixing time and stirrer speed were evaluated at lab scale (1 l) with two different system compositions. Stirrer speed between 400 and 800 rpm and mixing time between 2 and 5 min led to the highest recoveries of cutinase. In all cases, inclusive of pilot scale (30 l), the equilibrium was reached after a few minutes. The performance of ATPS was reproducible within the scale range of 0.010–30 l and provided a standard deviation of the yield lower than 8%, leading to (i) a partition coefficient over 50, (ii) a yield over 95% and (iii) a concentration factor over 5. The fusion of the peptide (WP)4 to the cutinase protein enabled a 400 increase of the partition coefficient relative to the wild-type strain.

[1]  H. Hustedt,et al.  15 – Applications of Phase Partitioning in Biotechnology , 1985 .

[2]  M. Aires-Barros,et al.  Cutinase: from molecular level to bioprocess development. , 1999, Biotechnology and bioengineering.

[3]  S. Nagata Mixing: Principles and Applications , 1975 .

[4]  N. Karanth,et al.  Aqueous two phase extraction for downstream processing of enzymes/proteins. , 1995 .

[5]  J T Hsu,et al.  Aqueous two-phase systems for biomolecule separation. , 1992, Advances in biochemical engineering/biotechnology.

[6]  M. M. Bradford A rapid and sensitive method for the quantitation of microgram quantities of protein utilizing the principle of protein-dye binding. , 1976, Analytical biochemistry.

[7]  Fritz Ullmann,et al.  Ullmanns Encyklopädie der technischen Chemie , 1951 .

[8]  Raquel Aires-Barros,et al.  Large-scale extraction of proteins , 2002, Molecular biotechnology.

[9]  H. Hustedt,et al.  Purification of enzymes by liquid-liquid extraction , 1982 .

[10]  F. Tjerneld Aqueous Two-Phase Partitioning on an Industrial Scale , 1992 .

[11]  J. Asenjo,et al.  Kinetics of phase separation for polyethylene glycol–phosphate two‐phase systems , 1995, Biotechnology and bioengineering.

[12]  M. Aires-Barros,et al.  Fusarium solani pisi recombinant cutinase partitioning in peg/potassium phosphate aqueous two-phase systems , 1993 .

[13]  M. Aires-Barros,et al.  Partitioning of recombinant Fusarium solani pisi cutinase in polyethylene glycol-aqueous salt solution two-phase systems , 1994 .

[14]  M. Kula Trends and future prospects of aqueous two-phase extraction. , 1990, Bioseparation.

[15]  H. Hustedt,et al.  Phase equilibration in agitated vessels during extractive enzyme recovery , 1985 .

[16]  M. Kula,et al.  Recycling of salts in partition protein extraction processes. , 2007, Journal of chemical technology and biotechnology.

[17]  D. Reifsnyder,et al.  Large Scale, In Situ Isolation of Periplasmic IGF–I from E. coli , 1994, Bio/Technology.