The liquid-liquid extractive fermentation of L–lactic acid in a novel semi-partition bioreactor (SPB)

• Published in: Journal of biotechnology Vol. 360; pp. 55 - 61
• Main Authors: Teke, George M., Gakingo, Godfrey K., Pott, Robert W.M.
• Format: Journal Article
• Language: English
• Published: Netherlands Elsevier B.V 10.12.2022
• Subjects: Bioreactors; Fermentation; in situ product removal (ISPR); Lactic Acid; Liquid-Liquid Extraction; L–lactic acid (LA); Product inhibition; Semi-partition bioreactor (SPB); in situ product removal (ISPR); Semi-partition bioreactor (SPB); Product inhibition; Fermentation; L–lactic acid (LA); Liquid‐liquid extraction
• ISSN: 0168-1656; 1873-4863
• DOI: 10.1016/j.jbiotec.2022.10.017

Fermentation technology is commonly used as a mature process to produce numerous products with the help of micro-organisms. However, these organisms are sometimes inhibited by the accumulation of these products or their by-products. One route to circumvent this is via extractive fermentation, which combines the fermentation process with extraction. To facilitate this, novel bioreactor designs are required, such as the semi-partition bioreactor (SPB) which has been recently proposed for in-situ extractive fermentation. The latter combines a fermentation and an extraction unit into a single vessel using a mixer-settler principle. Where the bioproduct is produced in the mixer and removed continuous in the settler. As the SPB functionality is a subject of interest, this study builds on demonstrating different process conditions in the production of a sample bioprocess (lactic acid (LA)) which is susceptible to product inhibition. The results showed a 34.5 g/L LA concentration was obtained in the pH-controlled condition. While LA production can suffer from product inhibition, neutralizing agents can be easily used to curb inhibitory problems, however, the LA fermentation is a simple (and well-studied) example, which can demonstrate an alternative route to avoiding product inhibition (for systems which cannot be rescued using pH control). Hence, to replicate a scenario of product inhibition, two different process conditions were investigated, no pH control with no extraction (non-integrated), and no pH control with integrated extractive fermentation. Key findings showed higher LA concentration in integrated (25.10 g/L) as compared to the non-integrated (14.94 g/L) case with improved yield (0.75 gg−1 (integrated) versus 0.60 gg−1 (non-integrated)) and overall productivity (0.35 gL−1h−1(integrated) versus 0.20 gL−1h−1(non-integrated)) likewise. This is the first demonstration of an SP bioreactor, and shows how the reactor can be applied to improve productivity. Based on these results, the SPB design can be applied to produce any product liable to product inhibition. [Display omitted] •Production of a sample bioproduct (lactic acid) has been illustrated in the SPB.•A 1.7 fold improved LA concentration was achieved in the integrated SPB design.•A 25 % yield and 75 % productivity increment were recorded in the integrated SPB design.•Results affirm the SPB design purpose of an extractive fermentation bioreactor.