## Abstract A key step in a chemoenzymatic process for the production of high‐purity glycolic acid (GLA) is the enzymatic conversion of glycolonitrile (GLN) to ammonium glycolate using a nitrilase derived from __Acidovorax facilis__ 72W. Protein engineering and over‐expression of this nitrilase, co
Optimization of Biocatalyst Specific Activity for Glycolic Acid Production
✍ Scribed by Arie Ben-Bassat; Alison M. Walls; Matthew A. Plummer; Amy E. Sigmund; William L. Spillan; Robert DiCosimo
- Publisher
- John Wiley and Sons
- Year
- 2008
- Tongue
- English
- Weight
- 280 KB
- Volume
- 350
- Category
- Article
- ISSN
- 1615-4150
No coin nor oath required. For personal study only.
✦ Synopsis
Abstract
A chemoenzymatic process has been developed that employs an immobilized microbial nitrilase biocatalyst for the conversion of glycolonitrile to high‐purity glycolic acid. The specific activity of this immobilized cell biocatalyst decreased significantly during initial use in either consecutive batch reactions with catalyst recycle, or in a continuous stirred‐tank reactor, but the nitrilase activity remaining after this initial decrease was stable under the reactions conditions. The initial stability of this immobilized cell nitrilase catalyst has been improved by treatment of the microbial cells with glutaraldehyde prior to immobilization. Conditions for glutaraldehyde treatment were defined that completely inactivated the culture without significantly affecting nitrilase activity. A method for dehydration, storage and rehydration of the carrageenan‐immobilized cells has also been demonstrated that further improves the specific activity of this biocatalyst.
📜 SIMILAR VOLUMES
The optimal feed rate profiles of glucose and ammonium hydroxide were calculated using a proposed model, and implemented for the production of poly-hydroxybutyric acid (PHB) by Alcaligenes eutrophus. By implementing these optimal feed rates with a high glucose feed concentration of 700 g/L and an a
## Abstract In this work, we considered a multistage integrated continuous fermentation process for producing lactic acid. Each stage consists of a mixing tank, a bioreactor, a cell‐recycle unit, and an extractor. A generalized mathematical model was formulated to express the integrated process. We