Expanded Bed Adsorption of γ‐Aminobutyric Acid from E. coli broth by CS16GC and IRC747 Resins

• Published in: Chemical engineering & technology Vol. 41; no. 12; pp. 2427 - 2434
• Main Authors: Pathapati, Trinath, Rütze, Dennis N., Boer, Piet, Wit, Pieter, Zaalberg, Menne
• Format: Journal Article
• Language: English
• Published: Germany Wiley Subscription Services, Inc 01.12.2018; John Wiley and Sons Inc
• Subjects: Adsorption; Cation exchanging; E coli; Expanded beds; Expanded‐bed adsorption; Fermentation; Fermentation broth; Flow distribution; Fluid dynamics; Fluid flow; Hydrodynamics; Ion exchange; Organic acids; Polymers; Resins; Uniform flow; γ‐Aminobutyric acid; Fermentation broth; Ion exchange; Expanded‐bed adsorption; γ‐Aminobutyric acid; Organic acids
• ISSN: 0930-7516; 1521-4125
• DOI: 10.1002/ceat.201800295

Expanded‐bed adsorption (EBA) is an efficient downstream technology that enhances the techno‐economic potential of bio‐based industries. However, application of EBA for bulk biochemicals requires the use of industrial resins. Therefore, two cation exchangers, namely, gel‐type CS16GC and porous IRC747, were tested to purify γ‐aminobutyric acid (GABA) from unclarified E. coli fermentation broth. Experiments compared the impact of gel‐type and macroporous resin properties on the EBA process performance. As an outcome, the gel‐type resin exhibited higher GABA binding capacity of compared to that of macroporous resin. This was due to improved hydrodynamics and uniform flow distribution in the case of gel‐type resin. Further, CS16GC effectively removed ≥ 99 % of impurities and achieved ≥ 97 % GABA yield. The techno‐economic potential of bio‐based industries can be improved by expanded‐bed adsorption as an efficient downstream technology. Industrial resins are required in order to apply this technique for bulk biochemicals. A gel‐type and a macroporous cation‐exchanger were tested to purify γ‐aminobutyric acid from unclarified E. coli fermentation broth. The former exhibited higher binding capacity.