Daniele Saluti Nunes de Barros , Vanessa Alves Lima Rocha , Camilla Pires de Souza , Rui de Paula Vieira de Castro , Manuela Moore Cardoso , Gabriela Coelho Brêda , Érika Cristina Gonçalves Aguieiras , Denise Maria Guimarães Freire
{"title":"生物炼制方法中酒糟干谷物固体发酵生产脂肪酶:优化和技术经济分析","authors":"Daniele Saluti Nunes de Barros , Vanessa Alves Lima Rocha , Camilla Pires de Souza , Rui de Paula Vieira de Castro , Manuela Moore Cardoso , Gabriela Coelho Brêda , Érika Cristina Gonçalves Aguieiras , Denise Maria Guimarães Freire","doi":"10.1016/j.biteb.2024.102015","DOIUrl":null,"url":null,"abstract":"<div><div>This work proposes a biorefinery process from the corn ethanol industry to produce a low-cost dry-fermented solid biocatalyst and enzymatic biodiesel. The fermentation conditions (temperature, moisture, and spore concentration) were optimized through a design experiment. In the best conditions (27 °C, 65 % moisture content, and 1.00 × 10<sup>7</sup> spores from <em>Rhizopus oryzae</em>/g of solid), it was possible to obtain 80 % conversion of oleic acid and ethanol to ester in 24 h of reaction. A solid pre-inoculum strategy was used to scale up the biocatalyst production by 100 times. The simulation in three different scenarios and its techno-economic analysis – made using the software SuperPro Designer – answered questions related to the feasibility of the biocatalyst production. In the best scenario, the unitary production cost was US$ 3.47/kg. Selling this product for US$ 7.30/kg would represent more than 100 % profit and a payback time of 1.46 years.</div></div>","PeriodicalId":8947,"journal":{"name":"Bioresource Technology Reports","volume":"29 ","pages":"Article 102015"},"PeriodicalIF":0.0000,"publicationDate":"2025-02-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Lipase production by solid-state fermentation on distiller's dried grain with solubles in a biorefinery approach: Optimization and techno-economic analysis\",\"authors\":\"Daniele Saluti Nunes de Barros , Vanessa Alves Lima Rocha , Camilla Pires de Souza , Rui de Paula Vieira de Castro , Manuela Moore Cardoso , Gabriela Coelho Brêda , Érika Cristina Gonçalves Aguieiras , Denise Maria Guimarães Freire\",\"doi\":\"10.1016/j.biteb.2024.102015\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>This work proposes a biorefinery process from the corn ethanol industry to produce a low-cost dry-fermented solid biocatalyst and enzymatic biodiesel. The fermentation conditions (temperature, moisture, and spore concentration) were optimized through a design experiment. In the best conditions (27 °C, 65 % moisture content, and 1.00 × 10<sup>7</sup> spores from <em>Rhizopus oryzae</em>/g of solid), it was possible to obtain 80 % conversion of oleic acid and ethanol to ester in 24 h of reaction. A solid pre-inoculum strategy was used to scale up the biocatalyst production by 100 times. The simulation in three different scenarios and its techno-economic analysis – made using the software SuperPro Designer – answered questions related to the feasibility of the biocatalyst production. In the best scenario, the unitary production cost was US$ 3.47/kg. Selling this product for US$ 7.30/kg would represent more than 100 % profit and a payback time of 1.46 years.</div></div>\",\"PeriodicalId\":8947,\"journal\":{\"name\":\"Bioresource Technology Reports\",\"volume\":\"29 \",\"pages\":\"Article 102015\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"2025-02-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Bioresource Technology Reports\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S2589014X24002561\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q1\",\"JCRName\":\"Environmental Science\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Bioresource Technology Reports","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S2589014X24002561","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"Environmental Science","Score":null,"Total":0}
Lipase production by solid-state fermentation on distiller's dried grain with solubles in a biorefinery approach: Optimization and techno-economic analysis
This work proposes a biorefinery process from the corn ethanol industry to produce a low-cost dry-fermented solid biocatalyst and enzymatic biodiesel. The fermentation conditions (temperature, moisture, and spore concentration) were optimized through a design experiment. In the best conditions (27 °C, 65 % moisture content, and 1.00 × 107 spores from Rhizopus oryzae/g of solid), it was possible to obtain 80 % conversion of oleic acid and ethanol to ester in 24 h of reaction. A solid pre-inoculum strategy was used to scale up the biocatalyst production by 100 times. The simulation in three different scenarios and its techno-economic analysis – made using the software SuperPro Designer – answered questions related to the feasibility of the biocatalyst production. In the best scenario, the unitary production cost was US$ 3.47/kg. Selling this product for US$ 7.30/kg would represent more than 100 % profit and a payback time of 1.46 years.