|
|
|
|
LEADER |
02963nam a2200469Ia 4500 |
001 |
0.3390-en15072600 |
008 |
220421s2022 CNT 000 0 und d |
020 |
|
|
|a 19961073 (ISSN)
|
245 |
1 |
0 |
|a High Solid and Low Cellulase Enzymatic Hydrolysis of Cardoon Stems Pretreated by Acidified Γ-Valerolactone/Water Solution
|
260 |
|
0 |
|b MDPI
|c 2022
|
856 |
|
|
|z View Fulltext in Publisher
|u https://doi.org/10.3390/en15072600
|
520 |
3 |
|
|a Lignocellulosic biomass is a nonedible matrix that can be efficiently exploited as feedstock in an integrated biorefinery after a proper pretreatment. An organosolv pretreatment using an acidified γ-valerolactone (GVL)/water solution was proposed to improve the cellulose enrichment and enzymatic saccharification of cardoon (Cynara cardunculus L.) stems. At the optimal pretreatment condition (140◦C, 0.6 GVL/water, and 2.24% H2SO4), xylan was efficiently removed from the cardoon, and up to 50% of its content was recovered in the aqueous fraction, while 86% of the cellulose was retained in the solid fraction. The resulting cardoon pulp showed a cellulose content of 91.5% and an enzymatic digestibility of 100%. An overall glucose production of 37.17 g/100 g raw material (90% theoretical maximum) was obtained using high solid loading (20% w/w) and a high enzyme dosage (60 FPU/g cellulose). At a low enzyme dosage, glucose concentrations of 169 g/L and 210 g/L were achieved using 10 FPU/g cellulose and 20 FPU/g cellulose, respectively. Therefore, an organosolv pretreatment can be an effective process for producing cellulose-enriched pulp with enhanced enzymatic digestibility from cardoon stems, providing a promising option for green lignocellulosic biorefineries that aim to produce high concentrations of glucose with low cellulase addition. © 2022 by the authors. Licensee MDPI, Basel, Switzerland.
|
650 |
0 |
4 |
|a Cellulose
|
650 |
0 |
4 |
|a cellulose enrichment
|
650 |
0 |
4 |
|a Cellulose enrichment
|
650 |
0 |
4 |
|a Cynara cardunculus
|
650 |
0 |
4 |
|a Cynara cardunculus
|
650 |
0 |
4 |
|a Delignification
|
650 |
0 |
4 |
|a Enzymatic hydrolysis
|
650 |
0 |
4 |
|a Glucose
|
650 |
0 |
4 |
|a High solid loading
|
650 |
0 |
4 |
|a high solid loading enzymatic hydrolysis
|
650 |
0 |
4 |
|a High solid loading enzymatic hydrolysis
|
650 |
0 |
4 |
|a low cellulase addition
|
650 |
0 |
4 |
|a Low cellulase addition
|
650 |
0 |
4 |
|a Microwave-assisted extraction
|
650 |
0 |
4 |
|a microwave-assisted extraction (MAE)
|
650 |
0 |
4 |
|a Organosolv pretreatment
|
650 |
0 |
4 |
|a Refining
|
650 |
0 |
4 |
|a Saccharification
|
650 |
0 |
4 |
|a Water solutions
|
650 |
0 |
4 |
|a γ-valerolactone/water delignification
|
650 |
0 |
4 |
|a Γ-valerolactone/water delignification
|
700 |
1 |
0 |
|a Cavalaglio, G.
|e author
|
700 |
1 |
0 |
|a Coccia, V.
|e author
|
700 |
1 |
0 |
|a Fabbrizi, G.
|e author
|
700 |
1 |
0 |
|a Gelosia, M.
|e author
|
700 |
1 |
0 |
|a Giannoni, T.
|e author
|
700 |
1 |
0 |
|a Iodice, P.
|e author
|
700 |
1 |
0 |
|a Lorenzi, L.
|e author
|
700 |
1 |
0 |
|a Nicolini, A.
|e author
|
773 |
|
|
|t Energies
|