Bioproduction of cis-(1S,2R)-indandiol, a chiral pharmaceutical intermediate, using a solid-liquid two-phase partitioning bioreactor for enhanced removal of inhibitors

• Published in: Journal of chemical technology and biotechnology (1986) 2011-11, Vol.86 (11), p.1379-1385
• Main Authors: Dafoe, Julian T S, Daugulis, Andrew J
• Format: Article
• Language: English
• Subjects: Applied sciences; Beads; Biological and medical sciences; Bioreactors; Biotechnology; Biotransformation; Chemical engineering; Exact sciences and technology; Fundamental and applied biological sciences. Psychology; indandiol; indene bioconversion; Inhibitors; Liquids; Methods. Procedures. Technologies; Others; Partitioning; polymer beads; Productivity; Pseudomonas putida; Reactors; Toxicity; two-phase partitioning bioreactor; Various methods and equipments
• ISSN: 0268-2575; 1097-4660; 1097-4660
• DOI: 10.1002/jctb.2653

BACKGROUND: A solid‐liquid two‐phase partitioning bioreactor (TPPB) was used in the biotransformation of indene to cis‐(1S,2R)‐indandiol by Pseudomonas putida 421‐5 (ATCC 55687). Metered substrate feeding in single‐phase operation, or delivery from an immiscible liquid, have previously been employed to regulate the exposure of the biocatalyst to inhibitory concentrations of the substrate. In contrast, the solid‐liquid platform provided in situ substrate addition (ISSA) as well as simultaneous it in situ product removal (ISPR) as a means of overcoming substrate and product toxicity. Three different modes of operation were compared for their effects on the performance of this biotransformation: single‐phase, fed‐batch operation was carried out as a benchmark in 2.75 L aqueous medium, and subsequently with the inclusion of either 700 g liquid silicone oil or 700 g solid polymer beads. RESULTS: Biphasic modes achieved a 3‐fold productivity improvement with respect to single‐phase (30 to 90 mg L−1 h−1), and solid‐liquid productivity was similar to liquid‐liquid operation while achieving more extensive removal of inhibitory compounds resulting in a slightly higher product titer (1.29 vs 1.16 g L−1). The operability of the reactor was improved by the phase stability of the solid polymer beads relative to immiscible organic solvents, preventing emulsion formation and facilitating analytics. CONCLUSION: Solid polymer beads replaced the immiscible liquid auxiliary phase for substrate delivery while performing simultaneous inhibitory molecule sequestration. Copyright © 2011 Society of Chemical Industry