## Abstract The biotransformation of toluene to 3‐methycatechol (3MC) via __Pseudomonas putida__ MC2 was used as a model system for the development of a biphasic process offering enhanced overall volumetric productivity. Three factors were investigated for the identification of an appropriate organ
A novel solid–liquid two-phase partitioning bioreactor for the enhanced bioproduction of 3-methylcatechol
✍ Scribed by George P. Prpich; Andrew J. Daugulis
- Publisher
- John Wiley and Sons
- Year
- 2007
- Tongue
- English
- Weight
- 152 KB
- Volume
- 98
- Category
- Article
- ISSN
- 0006-3592
No coin nor oath required. For personal study only.
✦ Synopsis
Abstract
The bioproduction of 3‐methylcatechol from toluene via Pseudomonas putida MC2 was performed in a solid–liquid two‐phase partitioning bioreactor with the intent of increasing yield and productivity over a single‐phase system. The solid phase consisted of HYTREL™, a thermoplastic polymer that was shown to possess superior affinity for the inhibitory 3‐methylcatechol compared to other candidate polymers as well as a number of immiscible organic solvents. Operation of a solid–liquid biotransformation utilizing a 10% (w/w) solid (polymer beads) to liquid phase ratio resulted in the bioproduction of 3‐methylcatechol at a rate of 350 mg/L‐h, which compares favorably to the single phase productivity of 128 mg/L‐h. . HYTREL™ polymer beads were also reconstituted into polymer sheets, which were placed around the interior circumference of the bioreactor and successfully removed 3‐methylcatechol from solution resulting in a rate of 3‐methylcatechol production of 343 mg/L‐h. Finally, a continuous biotransformation was performed in which culture medium was circulated upwards through an external extraction column containing HYTREL™ beads. The design maintained sub lethal concentrations of 3‐methylcatechol within the bioreactor by absorbing produced 3‐methylcatechol into the polymer beads. As 3‐methylcatechol concentrations in the aqueous phase approached 500 mg/L the extraction column was replaced (twice) with a fresh column and the process was continued representing a simple and effective approach for the continuous bioproduction of 3‐methylcatechol. Recovery of 3‐methylcatechol from HYTREL™ was also achieved by bead desorption into methanol. Biotechnol. Bioeng. 2007; 98: 1008–1016. © 2007 Wiley Periodicals, Inc.
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