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A novel close-circulating vapor stripping-vapor permeation technique for boosting biobutanol production and recovery
BACKGROUND: Butanol derived from renewable resources by microbial fermentation is considered as one of not only valuable platform chemicals but alternative advanced biofuels. However, due to low butanol concentration in fermentation broth, butanol production is restricted by high energy consumption...
Autores principales: | , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
BioMed Central
2018
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC5934881/ https://www.ncbi.nlm.nih.gov/pubmed/29755587 http://dx.doi.org/10.1186/s13068-018-1129-5 |
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author | Zhu, Chao Chen, Lijie Xue, Chuang Bai, Fengwu |
author_facet | Zhu, Chao Chen, Lijie Xue, Chuang Bai, Fengwu |
author_sort | Zhu, Chao |
collection | PubMed |
description | BACKGROUND: Butanol derived from renewable resources by microbial fermentation is considered as one of not only valuable platform chemicals but alternative advanced biofuels. However, due to low butanol concentration in fermentation broth, butanol production is restricted by high energy consumption for product recovery. For in situ butanol recovery techniques, such as gas stripping and pervaporation, the common problem is their low efficiency in harvesting and concentrating butanol. Therefore, there is a necessity to develop an advanced butanol recovery technique for cost-effective biobutanol production. RESULTS: A close-circulating vapor stripping-vapor permeation (VSVP) process was developed with temperature-difference control for single-stage butanol recovery. In the best scenario, the highest butanol separation factor of 142.7 reported to date could be achieved with commonly used polydimethylsiloxane membrane, when temperatures of feed solution and membrane surroundings were 70 and 0 °C, respectively. Additionally, more ABE (31.2 vs. 17.7 g/L) were produced in the integrated VSVP process, with a higher butanol yield (0.21 vs. 0.17 g/g) due to the mitigation of butanol inhibition. The integrated VSVP process generated a highly concentrated permeate containing 212.7 g/L butanol (339.3 g/L ABE), with the reduced energy consumption of 19.6 kJ/g-butanol. CONCLUSIONS: Therefore, the present study demonstrated a well-designed energy-efficient technique named by vapor stripping-vapor permeation for single-stage butanol removal. The butanol separation factor was multiplied by the temperature-difference control strategy which could double butanol recovery performance. This advanced VSVP process can completely eliminate membrane fouling risk for fermentative butanol separation, which is superior to other techniques. ELECTRONIC SUPPLEMENTARY MATERIAL: The online version of this article (10.1186/s13068-018-1129-5) contains supplementary material, which is available to authorized users. |
format | Online Article Text |
id | pubmed-5934881 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2018 |
publisher | BioMed Central |
record_format | MEDLINE/PubMed |
spelling | pubmed-59348812018-05-11 A novel close-circulating vapor stripping-vapor permeation technique for boosting biobutanol production and recovery Zhu, Chao Chen, Lijie Xue, Chuang Bai, Fengwu Biotechnol Biofuels Research BACKGROUND: Butanol derived from renewable resources by microbial fermentation is considered as one of not only valuable platform chemicals but alternative advanced biofuels. However, due to low butanol concentration in fermentation broth, butanol production is restricted by high energy consumption for product recovery. For in situ butanol recovery techniques, such as gas stripping and pervaporation, the common problem is their low efficiency in harvesting and concentrating butanol. Therefore, there is a necessity to develop an advanced butanol recovery technique for cost-effective biobutanol production. RESULTS: A close-circulating vapor stripping-vapor permeation (VSVP) process was developed with temperature-difference control for single-stage butanol recovery. In the best scenario, the highest butanol separation factor of 142.7 reported to date could be achieved with commonly used polydimethylsiloxane membrane, when temperatures of feed solution and membrane surroundings were 70 and 0 °C, respectively. Additionally, more ABE (31.2 vs. 17.7 g/L) were produced in the integrated VSVP process, with a higher butanol yield (0.21 vs. 0.17 g/g) due to the mitigation of butanol inhibition. The integrated VSVP process generated a highly concentrated permeate containing 212.7 g/L butanol (339.3 g/L ABE), with the reduced energy consumption of 19.6 kJ/g-butanol. CONCLUSIONS: Therefore, the present study demonstrated a well-designed energy-efficient technique named by vapor stripping-vapor permeation for single-stage butanol removal. The butanol separation factor was multiplied by the temperature-difference control strategy which could double butanol recovery performance. This advanced VSVP process can completely eliminate membrane fouling risk for fermentative butanol separation, which is superior to other techniques. ELECTRONIC SUPPLEMENTARY MATERIAL: The online version of this article (10.1186/s13068-018-1129-5) contains supplementary material, which is available to authorized users. BioMed Central 2018-05-04 /pmc/articles/PMC5934881/ /pubmed/29755587 http://dx.doi.org/10.1186/s13068-018-1129-5 Text en © The Author(s) 2018 Open AccessThis article is distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution, and reproduction in any medium, provided you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made. The Creative Commons Public Domain Dedication waiver (http://creativecommons.org/publicdomain/zero/1.0/) applies to the data made available in this article, unless otherwise stated. |
spellingShingle | Research Zhu, Chao Chen, Lijie Xue, Chuang Bai, Fengwu A novel close-circulating vapor stripping-vapor permeation technique for boosting biobutanol production and recovery |
title | A novel close-circulating vapor stripping-vapor permeation technique for boosting biobutanol production and recovery |
title_full | A novel close-circulating vapor stripping-vapor permeation technique for boosting biobutanol production and recovery |
title_fullStr | A novel close-circulating vapor stripping-vapor permeation technique for boosting biobutanol production and recovery |
title_full_unstemmed | A novel close-circulating vapor stripping-vapor permeation technique for boosting biobutanol production and recovery |
title_short | A novel close-circulating vapor stripping-vapor permeation technique for boosting biobutanol production and recovery |
title_sort | novel close-circulating vapor stripping-vapor permeation technique for boosting biobutanol production and recovery |
topic | Research |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC5934881/ https://www.ncbi.nlm.nih.gov/pubmed/29755587 http://dx.doi.org/10.1186/s13068-018-1129-5 |
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