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Development of an efficient simulated-moving-bed adsorption process for separation of 1,3-propanediol and glycerol coming from cyanobacterial fermentation based on photosynthesis and Calvin cycle

Authors
Woo, HyeongjooKang, Hoe-JongMun, Sungyong
Issue Date
Oct-2025
Publisher
ELSEVIER
Citation
SEPARATION AND PURIFICATION TECHNOLOGY, v.369, pp 1 - 14
Pages
14
Indexed
SCIE
SCOPUS
Journal Title
SEPARATION AND PURIFICATION TECHNOLOGY
Volume
369
Start Page
1
End Page
14
URI
https://scholarworks.bwise.kr/hanyang/handle/2021.sw.hanyang/210699
DOI
10.1016/j.seppur.2025.133043
ISSN
1383-5866
1873-3794
Abstract
With regard to microbial fermentation for the production of 1,3-propanediol (called “PDO” hereafter), there has been a particular interest in Calvin cycle-based cyanobacterium fermentation method, which has the advantage of not producing by-products other than PDO. To activate the industrial production of PDO based on this method, it is essential to establish a reliable process that can efficiently separate “PDO produced through reduction of glycerol” from “unreduced glycerol”. In response to this issue, this study aimed to investigate the possibility of applying a simulated-moving-bed (SMB) technology to the continuous separation of PDO from glycerol under the concentration ranges of PDO and glycerol formed through the considered fermentation processing. First, for such PDO-glycerol separation, it was found that the adsorbent consisting of only hydrophobic backbone could provide better selectivity than the type of adsorbents previously used (i.e., hydrophobic backbone-based cation exchange resins). Based on the adsorbent selected through this procedure, the intrinsic parameters of PDO and glycerol were determined and then utilized in the optimal design of the PDO-separation SMB process (called “PDO-SMB” hereafter). The results showed that a three-zone open-loop configuration based on the split of extract-port's upstream zone and separation zones was suitable for the PDO-SMB structure, under which its operating conditions were optimized in the direction of maximizing PDO yield and glycerol removal-rate. Through the operation of such optimized PDO-SMB process, the continuous separation of PDO from glycerol under the target concentration ranges was successfully achieved, which was confirmed both theoretically and experimentally. It was further found that the introduction of a two-substep operation mode and two extract ports into the PDO-SMB could help significantly improve the PDO-SMB productivity without reducing its separation performance.
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