Abstract:A mild borate assisted alkaline pretreatment was applied to Loblolly pine chips prior to kraft pulping to extract hemicelluloses. The extraction was performed at 90 °C for 4 h with 6% (w/w based on o.d. sample) alkali and 5% (w/w based on o.d. sample) boric acid. This process could recover 37.7% hemicellulose from the woodchips with only a 6.9% decrease in the cellulose degree of polymerization (DP). During the subsequent kraft pulping of the extracted woodchips, the process requires careful optimization to ob… Show more
“…These results suggest the possibility that the biomacromolecular "glue," between wood cells, which is primarily lignin, has been removed by pretreatment [43]. Figure 4 and Table 1 show a correlation between mass removal during pretreatment and sugar yield (glucose in Fig.…”
Section: Mannose/xylose Yieldmentioning
confidence: 87%
“…These regions are comprised mainly of lignin and pectin, with lesser amounts of hemicelluloses [43]. The morphological changes in loblolly pine with pretreatment can be seen in the SEM images presented in Fig.…”
Glycerol was used as a cosolvent with the two ionic l i q u i d s 1 -e t h y l -3 -m e t h y l i m i d a z o l i u m f o r m a t e ([C2mim][O2CH]) and 1-ethyl-3-methylimidazolium acetate ([C2mim][OAc]) to pretreat loblolly pine at 140°C. Enzymatic hydrolysis was then performed on raw and pretreated pines to establish pretreatment efficacy. With pretreatment, glucose yield from enzymatic hydrolysis was improved from 2 % for raw pine up to 43 %, while yields of mannose/xylose combined improved from 4 % up to 77 %. Pine pretreated with a 50 % [C2mim][O2CH]-50 % glycerol mixture exhibited a pulp-like structure, likely formed from removal of the lignin that binds cell walls together. Using this 50 % mixture of [C2mim][O2CH] and glycerol for pretreatment gave a slightly lower glucose yield than a 75 % mixture of [C2mim][O2CH] and glycerol but gave a mannose/xylose yield twice as high. Klason lignin and Fourier transform infrared spectroscopy (FTIR) analysis indicated that [C2mim][O2CH]-glycerol pretreatment preferentially dissolves lignin. FTIR analysis also suggested increased amorphous cellulose content with this pretreatment. Using the anti-solvent ethanol, a lignin-rich substance was precipitated from the solvent mixtures.
“…These results suggest the possibility that the biomacromolecular "glue," between wood cells, which is primarily lignin, has been removed by pretreatment [43]. Figure 4 and Table 1 show a correlation between mass removal during pretreatment and sugar yield (glucose in Fig.…”
Section: Mannose/xylose Yieldmentioning
confidence: 87%
“…These regions are comprised mainly of lignin and pectin, with lesser amounts of hemicelluloses [43]. The morphological changes in loblolly pine with pretreatment can be seen in the SEM images presented in Fig.…”
Glycerol was used as a cosolvent with the two ionic l i q u i d s 1 -e t h y l -3 -m e t h y l i m i d a z o l i u m f o r m a t e ([C2mim][O2CH]) and 1-ethyl-3-methylimidazolium acetate ([C2mim][OAc]) to pretreat loblolly pine at 140°C. Enzymatic hydrolysis was then performed on raw and pretreated pines to establish pretreatment efficacy. With pretreatment, glucose yield from enzymatic hydrolysis was improved from 2 % for raw pine up to 43 %, while yields of mannose/xylose combined improved from 4 % up to 77 %. Pine pretreated with a 50 % [C2mim][O2CH]-50 % glycerol mixture exhibited a pulp-like structure, likely formed from removal of the lignin that binds cell walls together. Using this 50 % mixture of [C2mim][O2CH] and glycerol for pretreatment gave a slightly lower glucose yield than a 75 % mixture of [C2mim][O2CH] and glycerol but gave a mannose/xylose yield twice as high. Klason lignin and Fourier transform infrared spectroscopy (FTIR) analysis indicated that [C2mim][O2CH]-glycerol pretreatment preferentially dissolves lignin. FTIR analysis also suggested increased amorphous cellulose content with this pretreatment. Using the anti-solvent ethanol, a lignin-rich substance was precipitated from the solvent mixtures.
“…[181][182][183] Two factors are vital in understanding the value of lignin in the biorefinery: the ease of lignin extraction, which is facilitated by treatments that reduce cross-linking to other cell wall polymers, and a structure that facilitates downstream processing. [184] Significant work has been focused on the [197] isolation of lignin from lignocellulosic biomass and depolymerization of lignin towards the production of biofuels and chemicals. [17,[185][186][187][188][189] Due to the extensive functionalities listed above, lignin-based carbon materials have been developed for energy storage, catalysis, and pollutant removal.…”
This publication is part of a joint Special Collection of Chemistry -Methods and ChemSusChem including invited contributions focusing on "Methods and Applications in Mechanochemistry". Please visit chemsuschem.org/ collections to view all contributions.
“…Furthermore, ideal bamboo-dissolving pulp with high brightness (92.4% ISO) and α-cellulose content (94.9%) has been obtained (Batalha et al 2012). Presently, a number of methods have been proposed for extracting hemicellulose in the prehydrolysis stage, including auto-hydrolysis (Leppänen et al 2011), dilute acid (Jeong et al 2010), mild alkali extraction (Huang and Ragauskas 2013), organic acid (Li et al 2010;Scordia et al 2011), and solid acid pretreatment (Dhepe and Sahu 2010). Among those methods, dilute acid extraction usually resulted in a lower pulp yield and physical properties, which were attributed to the acidity in the pretreatment medium (Aldajani et al 2009).…”
Section: Introductionmentioning
confidence: 99%
“…Among those methods, dilute acid extraction usually resulted in a lower pulp yield and physical properties, which were attributed to the acidity in the pretreatment medium (Aldajani et al 2009). According to Huang and Ragauskas (2013), the addition of boric acid (BA) in alkali solution can extract more hemicellulose from softwood and have little influence on cellulose.…”
Prehydrolysis is an important step in the kraft-based dissolving process for pulp production, as it helps remove as much hemicellulose as possible from cellulose fibers before the material is subjected to the main delignification operation, i.e., pulping. In this paper, a novel process concept was proposed by adding different dosages of boric acid (BA) based on the oven dry weight of Whangee, a genus of bamboo, in the prehydrolysis stage. The final yields of the prehydrolysis stage obviously increased and ferric ion contents in the hydrolyzed Whangee largely decreased with the addition of BA. Additionally, the highest α-cellulose retention occurred at a BA dosage of 0.5%. The results of acetic acid percent in the total sugars and furfural percent in xylose of the PHL showed that the addition of BA had an important impact on the structure of hemicelluloses in Whangee. Mass balance analysis of the PHL and Whangee indicated that the partly acid-insoluble lignin in Whangee was likely converted into acid-soluble lignin in the PHL.
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