{"title":"Pollution to Product—a Novel Two-Stage Single-Pot Fermentative Production of 1,3-Propanediol","authors":"Shreya Anand, Koel Mukherjee, Padmini Padmanabhan","doi":"10.1007/s12155-023-10570-1","DOIUrl":null,"url":null,"abstract":"<div><p>Many industrial chemicals are currently produced from fossil resources. However, extensive use of fossil fuels has resulted in an alarming array of energy and pollution-related challenges. The industrial chemicals that are produced from fossil resources could be produced alternatively using green route in a sustainable manner. Here we report the production of 1,3-propanediol (1,3-PDO) through fermentative route using sugarcane processing wastes (sugarcane bagasse). This study used the second-generation (2G) fermentable sugar (2G FS) recovered from the low-cost feedstock sugarcane bagasse as a substrate for 1,3-PDO production through a mixed culture fermentation in a single pot using <i>Saccharomyces cerevisiae</i> NCIM 3594 and <i>Klebsiella pneumoniae</i> NCIM 2957. This novel concept of single-pot, mixed culture fermentation method to produce 1,3-PDO was verified by optimizing process parameters like substrate concentration (2G FS), pH, and temperature. The concentration of 2G FS was varied in the range of 0.5–5% (V<sub>2G FS</sub>/V<sub>working volume</sub>), pH was varied between 6 and 7, and the temperature range was 30–37°C. The maximum production of 1,3-PDO was observed at the concentration of 5% (V<sub>2G FS</sub>/V<sub>working volume</sub>), at an optimum pH of 6.8 and a temperature of 35°C. The evaluated thermodynamics parameters for analyzing the rate of fermentation were enthalpy (Δ<i>H</i>), ?47596 KJ/mol; activation energy (Δ<i>E</i>), ?47596 KJ/mol; entropy (Δ<i>S</i>), 500.46 J/mol; and Gibbs free energy (Δ<i>G</i>), ?2.018?×?10<sup>5</sup>?J/mol; and the kinetics parameters were specific growth rate (<i>μ</i>), 0.0053 h<sup>?1</sup>; cell mass productivity (<i>Q</i><sub><i>x</i></sub>), 0.249 g/L<sup>/</sup>h; rate of production (<i>Q</i><sub><i>p</i></sub>), 0.237 g/L<sup>/</sup>h; and product yield (<i>Y</i><sub><i>p/s</i></sub>), 0.0427 g/g. This work demonstrates a novel single-pot method to produce 1,3-PDO from a low-cost feedstock and makes a valuable contribution to the development of a cost-effective fermentation based on renewable resources.</p></div>","PeriodicalId":487,"journal":{"name":"BioEnergy Research","volume":"16 3","pages":"1528 - 1536"},"PeriodicalIF":3.1000,"publicationDate":"2023-01-18","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://link.springer.com/content/pdf/10.1007/s12155-023-10570-1.pdf","citationCount":"1","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"BioEnergy Research","FirstCategoryId":"5","ListUrlMain":"https://link.springer.com/article/10.1007/s12155-023-10570-1","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
引用次数: 1
Abstract
Many industrial chemicals are currently produced from fossil resources. However, extensive use of fossil fuels has resulted in an alarming array of energy and pollution-related challenges. The industrial chemicals that are produced from fossil resources could be produced alternatively using green route in a sustainable manner. Here we report the production of 1,3-propanediol (1,3-PDO) through fermentative route using sugarcane processing wastes (sugarcane bagasse). This study used the second-generation (2G) fermentable sugar (2G FS) recovered from the low-cost feedstock sugarcane bagasse as a substrate for 1,3-PDO production through a mixed culture fermentation in a single pot using Saccharomyces cerevisiae NCIM 3594 and Klebsiella pneumoniae NCIM 2957. This novel concept of single-pot, mixed culture fermentation method to produce 1,3-PDO was verified by optimizing process parameters like substrate concentration (2G FS), pH, and temperature. The concentration of 2G FS was varied in the range of 0.5–5% (V2G FS/Vworking volume), pH was varied between 6 and 7, and the temperature range was 30–37°C. The maximum production of 1,3-PDO was observed at the concentration of 5% (V2G FS/Vworking volume), at an optimum pH of 6.8 and a temperature of 35°C. The evaluated thermodynamics parameters for analyzing the rate of fermentation were enthalpy (ΔH), ?47596 KJ/mol; activation energy (ΔE), ?47596 KJ/mol; entropy (ΔS), 500.46 J/mol; and Gibbs free energy (ΔG), ?2.018?×?105?J/mol; and the kinetics parameters were specific growth rate (μ), 0.0053 h?1; cell mass productivity (Qx), 0.249 g/L/h; rate of production (Qp), 0.237 g/L/h; and product yield (Yp/s), 0.0427 g/g. This work demonstrates a novel single-pot method to produce 1,3-PDO from a low-cost feedstock and makes a valuable contribution to the development of a cost-effective fermentation based on renewable resources.
期刊介绍:
BioEnergy Research fills a void in the rapidly growing area of feedstock biology research related to biomass, biofuels, and bioenergy. The journal publishes a wide range of articles, including peer-reviewed scientific research, reviews, perspectives and commentary, industry news, and government policy updates. Its coverage brings together a uniquely broad combination of disciplines with a common focus on feedstock biology and science, related to biomass, biofeedstock, and bioenergy production.