Production of Phenylacetylcarbinol via Biotransformation Using the Co-Culture of Candida tropicalis TISTR 5306 and Saccharomyces cerevisiae TISTR 5606 as the Biocatalyst

• Published in: Journal of fungi (Basel) Vol. 9; no. 9; p. 928
• Main Authors: Kumar, Anbarasu, Techapun, Charin, Sommanee, Sumeth, Mahakuntha, Chatchadaporn, Feng, Juan, Htike, Su Lwin, Khemacheewakul, Julaluk, Porninta, Kritsadaporn, Phimolsiripol, Yuthana, Wang, Wen, Zhuang, Xinshu, Qi, Wei, Jantanasakulwong, Kittisak, Nunta, Rojarej, Leksawasdi, Noppol
• Format: Journal Article
• Language: English
• Published: Switzerland MDPI AG 14.09.2023; MDPI
• Subjects: Alcohol; Bagasse; Benzaldehyde; Biocatalysts; bioethanol; Biofuels; Biomass; Bioreactors; Biotransformation; By products; Candida tropicalis; Carbon; Carbon sources; Cell culture; Cellulase; Chemical synthesis; Cost analysis; Enzymes; Ephedrine; Ethanol; Glucose; Hydrolysates; Microorganisms; phenylacetylcarbinol; Pyruvate decarboxylase; Pyruvic acid; Saccharomyces cerevisiae; Sugarcane; Yeast; Thailand; Candida tropicalis; biotransformation; bioethanol; phenylacetylcarbinol; Saccharomyces cerevisiae; pyruvate decarboxylase
• ISSN: 2309-608X; 2309-608X
• DOI: 10.3390/jof9090928

Phenylacetylcarbinol (PAC) is a precursor for the synthesis of several pharmaceuticals, including ephedrine, pseudoephedrine, and norephedrine. PAC is commonly produced through biotransformation using microbial pyruvate decarboxylase (PDC) in the form of frozen-thawed whole cells. However, the lack of microorganisms capable of high PDC activity is the main factor in the production of PAC. In addition, researchers are also looking for ways to utilize agro-industrial residues as an inexpensive carbon source through an integrated biorefinery approach in which sugars can be utilized for bioethanol production and frozen-thawed whole cells for PAC synthesis. In the present study, , , and the co-culture of both strains were compared for their biomass and ethanol concentrations, as well as for their volumetric and specific PDC activities when cultivated in a sugarcane bagasse (SCB) hydrolysate medium (SCBHM). The co-culture that resulted in a higher level of PAC (8.65 ± 0.08 mM) with 26.4 ± 0.9 g L ethanol production was chosen for further experiments. Biomass production was scaled up to 100 L and the kinetic parameters were studied. The biomass harvested from the bioreactor was utilized as frozen-thawed whole cells for the selection of an initial pyruvate (Pyr)-to-benzaldehyde (Bz) concentration ([Pyr]/[Bz]) ratio suitable for the PAC biotransformation in a single-phase emulsion system. The initial [Pyr]/[Bz] at 100/120 mM resulted in higher PAC levels with 10.5 ± 0.2 mM when compared to 200/240 mM (8.60 ± 0.01 mM). A subsequent two-phase emulsion system with Pyr in the aqueous phase, Bz in the organic phase, and frozen-thawed whole cells of the co-culture as the biocatalyst produced a 1.46-fold higher PAC level when compared to a single-phase emulsion system. In addition, the cost analysis strategy indicated preliminary costs of USD 0.82 and 1.01/kg PAC for the single-phase and two-phase emulsion systems, respectively. The results of the present study suggested that the co-culture of and can effectively produce bioethanol and PAC from SCB and would decrease the overall production cost on an industrial scale utilizing the two-phase emulsion system with the proposed multiple-pass strategy.