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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

邮发代号 80-969

2019 Impact Factor: 3.552

Frontiers of Chemical Science and Engineering  2024, Vol. 18 Issue (11): 139   https://doi.org/10.1007/s11705-024-2490-5
  本期目录
γ-Valerolactone/CuCl2 biphasic system for high total monosaccharides recovery from pretreatment and enzymatic hydrolysis processes of eucalyptus
Shuhua Mo, Yao Zheng, Jianyu Gong, Minsheng Lu()
Guangxi Key Laboratory of Clean Pulp & Papermaking and Pollution Control, School of Light Industrial and Food Engineering, Guangxi University, Nanning 530004, China
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Abstract

The efficient fractionation and recovery of monosaccharides (xylose and glucose) from lignocellulosic biomass facilitates subsequent sugar-based derivative production. This study introduces a one-pot γ-valerolactone/CuCl2 biphasic pretreatment system (100-mmol·L–1 CuCl2, 180 °C, 60 min) capable of achieving removal rates of 92.25% and 90.64% for xylan and lignin, respectively, while retaining 83.88% of cellulose. Compared to other metal chlorides (NaCl, LiCl, FeCl3, and AlCl3), the γ-valerolactone/CuCl2 system recovered 121.2 mg·(g eucalyptus)–1 of xylose and 55.96 mg·(g eucalyptus)–1 of glucose during the pretreatment stage and 339.2 mg·(g eucalyptus)–1 of glucose during the enzymatic hydrolysis stage (90.78% of glucose yield), achieving a total monosaccharide recovery of 86.31%. In addition, the recovery of γ-valerolactone was 79.33%, exhibiting minimal changes relative to the pretreatment performance. The method proposed in this study allows a high total monosaccharides recovery and a circular economy-oriented pretreatment approach, offering a viable pathway for biorefinery.

Key wordslignocellulose    biorefinery    total monosaccharides recovery    γ-valerolactone
收稿日期: 2024-03-15      出版日期: 2024-07-31
Corresponding Author(s): Minsheng Lu   
 引用本文:   
. [J]. Frontiers of Chemical Science and Engineering, 2024, 18(11): 139.
Shuhua Mo, Yao Zheng, Jianyu Gong, Minsheng Lu. γ-Valerolactone/CuCl2 biphasic system for high total monosaccharides recovery from pretreatment and enzymatic hydrolysis processes of eucalyptus. Front. Chem. Sci. Eng., 2024, 18(11): 139.
 链接本文:  
https://academic.hep.com.cn/fcse/CN/10.1007/s11705-024-2490-5
https://academic.hep.com.cn/fcse/CN/Y2024/V18/I11/139
Fig.1  
Fig.2  
Sample Cellulose/% Cellulose recovery/% Xylan/% Xylan removal/% Lignin/% Lignin removal/% Ash/% Solid yield/%
Raw 44.49 ± 0.12 15.33 ± 0.05 35.58 ± 1.07 0.21
SR-GVLa) 49.17 ± 0.73 94.83 14.55 ± 0.09 18.55 29.50 ± 0.42 28.85 0.54 85.81
SR-Cu2+b) 56.06 ± 0.01 86.30 1.94 ± 0.12 91.33 38.34 ± 0.38 26.19 0.38 68.49
SR-GVL/Cu2+ 86.07 ± 0.56 83.88 2.74 ± 0.41 92.25 7.68 ± 0.59 90.64 0.31 43.36
Tab.1  
Fig.3  
Fig.4  
Sample C/% O/% O/C SLC/% C1/% C2/% C3/% BET surface area/(m2·g–1) Porosity/%
Raw 68.92 29.39 0.43 80.80 58.41 31.98 9.60 0.82 41.67
SR-GVL 67.73 30.09 0.44 77.15 53.22 38.32 8.45 0.98 53.43
SR-Cu2+ 70.44 28.05 0.40 86.36 54.57 37.58 7.85 1.49 60.59
SR-GVL/Cu2+ 60.83 37.61 0.62 42.34 47.10 43.95 8.95 3.01 78.83
Tab.2  
Fig.5  
Sample Cellulose/% Cellulose recovery/% Xylan/% Xylan removal/% Lignin/% Lignin removal/% GVL recovery/%
Raw 44.49 ± 0.12 15.33 ± 0.05 35.58 ± 1.07
SR-GVL/Cu2+ 86.07 ± 0.56 83.88 2.74 ± 0.41 92.25 7.68 ± 0.59 90.64 79.33
SR-Recycle 1 84.31 ± 0.28 84.00 1.87 ± 0.15 94.59 8.79 ± 0.48 89.05 81.48
SR-Recycle 2 81.62 ± 0.56 84.67 1.95 ± 0.41 94.13 12.46 ± 0.30 83.84
Tab.3  
Sample Cellulose/% Cellulose recovery/% Xylan/% Xylan removal/% Lignin/% Lignin removal/% Ash/% Solid yield/%
Raw 44.49 ± 0.12 15.33 ± 0.05 35.58 ± 1.07 0.21
GVL/CuCl2 86.07 ± 0.56 83.88 2.74 ± 0.41 92.25 7.68 ± 0.59 90.64 0.31 43.36
GVL/FeCl3 85.05 ± 0.63 81.70 1.31 ± 0.13 96.35 7.27 ± 0.55 90.96 0.68 42.74
GVL/AlCl3 82.92 ± 0.74 71.36 2.16 ± 0.05 94.61 8.85 ± 0.84 90.48 0.44 38.29
GVL/NaCl 51.39 ± 1.02 94.13 14.03 ± 0.44 25.42 28.85 ± 1.33 33.92 0.33 81.49
GVL/LiCl 52.02 ± 0.36 92.24 13.33 ± 0.27 31.40 26.88 ± 0.47 40.40 0.52 78.89
Tab.4  
Fig.6  
Fig.7  
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