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...
Autores principales: | , , , , , , |
---|---|
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 |