Cargando…

A new approach to recycle oxalic acid during lignocellulose pretreatment for xylose production

BACKGROUND: Dilute oxalic acid pretreatment has drawn much attention because it could selectively hydrolyse the hemicellulose fraction during lignocellulose pretreatment. However, there are few studies focusing on the recovery of oxalic acid. Here, we reported a new approach to recycle oxalic acid u...

Descripción completa

Detalles Bibliográficos
Autores principales: Cheng, Banggui, Zhang, Xiao, Lin, Qixuan, Xin, Fengxue, Sun, Runcang, Wang, Xiaohui, Ren, Junli
Formato: Online Artículo Texto
Lenguaje:English
Publicado: BioMed Central 2018
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6280388/
https://www.ncbi.nlm.nih.gov/pubmed/30534202
http://dx.doi.org/10.1186/s13068-018-1325-3
_version_ 1783378659242934272
author Cheng, Banggui
Zhang, Xiao
Lin, Qixuan
Xin, Fengxue
Sun, Runcang
Wang, Xiaohui
Ren, Junli
author_facet Cheng, Banggui
Zhang, Xiao
Lin, Qixuan
Xin, Fengxue
Sun, Runcang
Wang, Xiaohui
Ren, Junli
author_sort Cheng, Banggui
collection PubMed
description BACKGROUND: Dilute oxalic acid pretreatment has drawn much attention because it could selectively hydrolyse the hemicellulose fraction during lignocellulose pretreatment. However, there are few studies focusing on the recovery of oxalic acid. Here, we reported a new approach to recycle oxalic acid used in pretreatment via ethanol extraction. RESULTS: The highest xylose content in hydrolysate was 266.70 mg xylose per 1 g corncob (85.0% yield), which was achieved using 150 mmol/L oxalic acid under the optimized treatment condition (140 °C, 2.5 h). These pretreatment conditions were employed to the subsequent pretreatment using recycled oxalic acid. Oxalic acid in the hydrolysate could be recycled according to the following steps: (1) water was removed via evaporation and vacuum drying, (2) ethanol was used to extract oxalic acid in the remaining mixture, and (3) oxalic acid and ethanol were separated by reduced pressure evaporation. The total xylose yields could be stabilized by intermittent adding oxalic acid, and the yields were in range of 46.7–64.3% in this experiment. CONCLUSIONS: This sustainable approach of recycling and reuse of oxalic acid has a significant potential application for replacing traditional dilute mineral acid pretreatment of lignocellulose, which could contribute to reduce CO(2) emissions and the cost of the pretreatment.
format Online
Article
Text
id pubmed-6280388
institution National Center for Biotechnology Information
language English
publishDate 2018
publisher BioMed Central
record_format MEDLINE/PubMed
spelling pubmed-62803882018-12-10 A new approach to recycle oxalic acid during lignocellulose pretreatment for xylose production Cheng, Banggui Zhang, Xiao Lin, Qixuan Xin, Fengxue Sun, Runcang Wang, Xiaohui Ren, Junli Biotechnol Biofuels Research BACKGROUND: Dilute oxalic acid pretreatment has drawn much attention because it could selectively hydrolyse the hemicellulose fraction during lignocellulose pretreatment. However, there are few studies focusing on the recovery of oxalic acid. Here, we reported a new approach to recycle oxalic acid used in pretreatment via ethanol extraction. RESULTS: The highest xylose content in hydrolysate was 266.70 mg xylose per 1 g corncob (85.0% yield), which was achieved using 150 mmol/L oxalic acid under the optimized treatment condition (140 °C, 2.5 h). These pretreatment conditions were employed to the subsequent pretreatment using recycled oxalic acid. Oxalic acid in the hydrolysate could be recycled according to the following steps: (1) water was removed via evaporation and vacuum drying, (2) ethanol was used to extract oxalic acid in the remaining mixture, and (3) oxalic acid and ethanol were separated by reduced pressure evaporation. The total xylose yields could be stabilized by intermittent adding oxalic acid, and the yields were in range of 46.7–64.3% in this experiment. CONCLUSIONS: This sustainable approach of recycling and reuse of oxalic acid has a significant potential application for replacing traditional dilute mineral acid pretreatment of lignocellulose, which could contribute to reduce CO(2) emissions and the cost of the pretreatment. BioMed Central 2018-12-05 /pmc/articles/PMC6280388/ /pubmed/30534202 http://dx.doi.org/10.1186/s13068-018-1325-3 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
Cheng, Banggui
Zhang, Xiao
Lin, Qixuan
Xin, Fengxue
Sun, Runcang
Wang, Xiaohui
Ren, Junli
A new approach to recycle oxalic acid during lignocellulose pretreatment for xylose production
title A new approach to recycle oxalic acid during lignocellulose pretreatment for xylose production
title_full A new approach to recycle oxalic acid during lignocellulose pretreatment for xylose production
title_fullStr A new approach to recycle oxalic acid during lignocellulose pretreatment for xylose production
title_full_unstemmed A new approach to recycle oxalic acid during lignocellulose pretreatment for xylose production
title_short A new approach to recycle oxalic acid during lignocellulose pretreatment for xylose production
title_sort new approach to recycle oxalic acid during lignocellulose pretreatment for xylose production
topic Research
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6280388/
https://www.ncbi.nlm.nih.gov/pubmed/30534202
http://dx.doi.org/10.1186/s13068-018-1325-3
work_keys_str_mv AT chengbanggui anewapproachtorecycleoxalicacidduringlignocellulosepretreatmentforxyloseproduction
AT zhangxiao anewapproachtorecycleoxalicacidduringlignocellulosepretreatmentforxyloseproduction
AT linqixuan anewapproachtorecycleoxalicacidduringlignocellulosepretreatmentforxyloseproduction
AT xinfengxue anewapproachtorecycleoxalicacidduringlignocellulosepretreatmentforxyloseproduction
AT sunruncang anewapproachtorecycleoxalicacidduringlignocellulosepretreatmentforxyloseproduction
AT wangxiaohui anewapproachtorecycleoxalicacidduringlignocellulosepretreatmentforxyloseproduction
AT renjunli anewapproachtorecycleoxalicacidduringlignocellulosepretreatmentforxyloseproduction
AT chengbanggui newapproachtorecycleoxalicacidduringlignocellulosepretreatmentforxyloseproduction
AT zhangxiao newapproachtorecycleoxalicacidduringlignocellulosepretreatmentforxyloseproduction
AT linqixuan newapproachtorecycleoxalicacidduringlignocellulosepretreatmentforxyloseproduction
AT xinfengxue newapproachtorecycleoxalicacidduringlignocellulosepretreatmentforxyloseproduction
AT sunruncang newapproachtorecycleoxalicacidduringlignocellulosepretreatmentforxyloseproduction
AT wangxiaohui newapproachtorecycleoxalicacidduringlignocellulosepretreatmentforxyloseproduction
AT renjunli newapproachtorecycleoxalicacidduringlignocellulosepretreatmentforxyloseproduction