Literature DB >> 34156516

A validated strategy to design efficient fermentation-industrial processes: agave spirit production.

J L Navarrete-Bolaños1, O Serrato-Joya2, H Chávez-Mireles2, F J Vicente-Magueyal2, H Jiménez-Islas2.   

Abstract

An industrial process is profitable when its individual unit operations are efficient and thus, this work shows a guideline for designing efficient fermentation-industrial processes for agave distilled production based on a sequential approach of optimization, beginning in the laboratory and followed by the adjustment of the variable values using the evolutionary operation method for successful process scaling. The results at the laboratory showed that a starter inoculum containing a 5 × 106 cells/mL mixture of Kluyveromyces marxianus, Clavispora lusitaniae, and Kluyveromyces marxianus var. drosophilarum strains in a bioreactor containing agave syrup with 120 g/L fermented sugar, processed at a constant temperature of 33 °C and 1.0 VVM aeration for 1.6 h, led to a fermented product with a 4.18% (v/v) alcohol content after 72 h of processing time. The scale-up process results showed that the best operating conditions at the pilot-plant level were a temperature of 35 °C and aeration at 1.0 VVM for 1.2 h, which led to a fermented product with a 4.22% (v/v) total alcohol content after 72 h of processing time. These represent similar performance values for both production processes, but each one worked with their specific values of process variables, which demonstrates that each level of production had its own specific values for process variables. The volatile compound analysis shows that both distilled products contained a similar profile of volatile components that provide fruity and ethereal aromatic notes pleasant to the palate. Therefore, the process design for agave spirit production at the semi-industrial level was successfully achieved.
© 2021. The Author(s), under exclusive licence to Springer-Verlag GmbH Germany, part of Springer Nature.

Entities:  

Keywords:  Design; Fermentation; Industrial; Laboratory; Process; Scale-up

Mesh:

Year:  2021        PMID: 34156516     DOI: 10.1007/s00449-021-02600-z

Source DB:  PubMed          Journal:  Bioprocess Biosyst Eng        ISSN: 1615-7591            Impact factor:   3.210


  6 in total

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Authors:  Carl-Fredrik Mandenius; Anders Brundin
Journal:  Biotechnol Prog       Date:  2008 Nov-Dec

2.  Strategy for biotechnological process design applied to the enzymatic hydrolysis of agave fructo-oligosaccharides to obtain fructose-rich syrups.

Authors:  Mauricio García-Aguirre; Victor A Sáenz-Alvaro; Mayra A Rodríguez-Soto; Francisco J Vicente-Magueyal; Enrique Botello-Alvarez; Hugo Jimenez-Islas; Marcela Cárdenas-Manríquez; Ramiro Rico-Martínez; Jose L Navarrete-Bolaños
Journal:  J Agric Food Chem       Date:  2009-11-11       Impact factor: 5.279

3.  An experimental strategy validated to design cost-effective culture media based on response surface methodology.

Authors:  J L Navarrete-Bolaños; M G Téllez-Martínez; R Miranda-López; H Jiménez-Islas
Journal:  Prep Biochem Biotechnol       Date:  2017-01-19       Impact factor: 2.162

4.  Use of evolutionary operation (EVOP) factorial design technique to develop a bioprocess using grease waste as a substrate for lipase production.

Authors:  Sunil Kumar; Nitin Katiyar; Priyanka Ingle; Sangeeta Negi
Journal:  Bioresour Technol       Date:  2011-01-05       Impact factor: 9.642

5.  Characterization of volatile compounds of Mezcal, an ethnic alcoholic beverage obtained from Agave salmiana.

Authors:  Antonio De León-Rodríguez; Lidia González-Hernández; Ana P Barba de la Rosa; Pilar Escalante-Minakata; Mercedes G López
Journal:  J Agric Food Chem       Date:  2006-02-22       Impact factor: 5.279

6.  Bioprocess scale-up/down as integrative enabling technology: from fluid mechanics to systems biology and beyond.

Authors:  Frank Delvigne; Ralf Takors; Rob Mudde; Walter van Gulik; Henk Noorman
Journal:  Microb Biotechnol       Date:  2017-08-14       Impact factor: 5.813

  6 in total

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