A review on the production and recovery of sugars from lignocellulosics for use in the synthesis of bioproducts
Introduction
In the upcoming decades, the replacement of fossil resources demands cost-effective and technically feasible solutions. Renewable carbon sources from lignocellulosic biomasses (LBs) are among the promising options (Canilha et al., 2012, Farmanbordar et al., 2020, Neumann et al., 2016, Santibáñez et al., 2020). LB is inexpensive, environmentally friendly, and one of the most abundant yet underutilized resources in the world (Anwar et al., 2014, Ravindran and Jaiswal, 2016, Tayyab et al., 2018). It mainly consists of cellulose (40–50% on average), hemicellulose (25–30%), lignin (15–20%), and traces of pectin, nitrogen, and inorganic compounds (Borges et al., 2014, Chen et al., 2017, Fonseca, 2015, Rojas et al., 2014). This biomass's high degree of polymerization makes its cell walls stable and difficult to degrade (Behera et al., 2014, Chaula et al., 2014). Thus, methods for converting plant material into monomeric sugars (mostly glucose from cellulose and xylose from xylan) are required for their further use as feedstocks in the production of a range of value-added products (Ravindran and Jaiswal, 2016). These procedures comprise pretreatment and enzymatic hydrolysis (EH) steps (Angarita et al., 2015, Batista et al., 2019; Burke et al., 2009a; Canilha et al., 2012; Delabona et al., 2013, Delabona et al., 2012; Furlan et al., 2012; Rodríguez-Zúñiga et al., 2015), which are generally undertaken in conjunction with downstream sugar-recovery to meet the target product attributes (Milessi-esteves et al., 2019).
Pretreatment is necessary to provide internal access to biomass by the enzymes that will be used in the hydrolysis stage, i.e., such process promotes enzyme and substrate interaction to stimulate the subsequent EH (Chandra et al., 2015, Michalska et al., 2012). Each pretreatment technology presents a different mechanism of action on the plant structure, inducing either physical or chemical modifications. Several approaches have been used for this process, such as autohydrolysis, acid hydrolysis, ammonia activation, kraft pulping, organic solvent pulping, hot water pretreatment, ammonia percolation, lime pretreatment, caustic solvent pulping, alkaline peroxide pretreatment, among other methods (Burke et al., 2009a, Burke, 2009b; Pourbafrani et al., 2014). The selection of a suitable pretreatment strategy depends on the LB source, economic viability, environmental sustainability of the process (minimizing chemical, heat, and power requirements) (Furlan et al., 2016, Kumar et al., 2009, Longati et al., 2018, Yu et al., 2016, Yu et al., 2015), formation of degradation byproducts, process yield, production scale, as well as configurations employed in the hydrolysis and further processing (Abo et al., 2019, Bhutto et al., 2017, Hendriks and Zeeman, 2009, Soltanian et al., 2020).
The first step in the EH process consists of breaking down cellulose and hemicellulose (containing xylan) into soluble oligosaccharides of glucose and xylose, respectively. Then, enzyme complexes are used to convert oligosaccharides to monomeric sugars suitable for fermentation or catalytic transformation to bioproducts (Burke et al., 2009b). This approach is designed to maximize enzyme performance, controlling the effect of inhibitors while optimizing hydrolysis rates and sugar yields (Burke et al., 2009a).
After obtaining monomeric sugars from lignocellulosics through an appropriate pretreatment method and EH, the material is recovered and purified to extract the desired sugar(s) (Kumar et al., 2017). Sugar recovery methods may include solid/liquid systems, chromatographic and membrane separations, ion exchange or crystallization, among others. These strategies can be applied to (1) separate the extracts from the non-treated biomass (physical separations); (2) recover the glucose and/or the xylose (the main monosaccharides resulting from the hydrolysis of the cellulosic and hemicellulosic fractions of the LB, respectively) (Poletto et al., 2020, Santibáñez et al., 2020) through purification approaches, aiming for their later use in the synthesis of a variety of products, including sugars, biofuels, and value-added chemicals. The use of the hexoses is widely known, but usage of pentose sugars is gaining more visibility in this realm as well, because of the opportunity to increase the sugar and process yields from lignocellulosics, since the hemicellulose stream was often underexploited after the LB hydrolysis (Geng et al., 2019, Vescovi et al., 2017). Nevertheless, like many other commercial processes, the overall development of these processes demands the tailoring of specific attributes of the sugar products required for different applications (Huang et al., 2010, Saini et al., 2020), considering throughput and purity targets and, when applicable, the scale-up of the process (Banerjee et al., 2012, Cheng et al., 2020, Koppram et al., 2013, Wang et al., 2016).
Here, we survey the peer-reviewed literature addressing the production of sugars from lignocellulosics, focusing on xylose use (with or without other sugars) as a substrate in the synthesis of biochemical products. Potential knowledge gaps and trends within this subject are also explored.
Section snippets
Literature searching and database building
We performed a systematic search (Romanelli et al., 2021b) of the peer-reviewed literature from the Web of Science platform (bibliographic resources - core collection: Science Citation Index Expanded (SCI-E) and Emerging Sources Citation Index (ESCI)), besides Scopus, CAB Direct, and SciELO platforms. We chose the SCI-E and ESCI databases within the Web of Science platform because the first one covers the majority of significant scientific results, as well as other online databases that also
Results and discussion
The components of the system for obtaining sugars from lignocellulosics and the resulting sugar-derived products that are present in our database are available in Table S3 (Supplementary Material).
Conclusions
This study revealed that some classical pretreatment methods (e.g., alkaline and acidolysis) are still among the most used methodologies for the initial processing of LB. However, the conditions used in these methods are aggressive, leading to the formation of degradation by-products, reducing cellulosic/hemicellulosic sugar yields, and requiring high levels of energy. Some other technologies, such as LHW and SE, were used to minimize some of these issues, mainly inhibitors and waste
Funding
This work was supported by “Fundação de Amparo à Pesquisa do Estado de São Paulo” (FAPESP) [grant numbers 2016/10636-8, 2019/23908-4, 2019/08533-4, 2021/06525-4, and 2021/07958-1]; in part by “Coordenação de Aperfeiçoamento de Pessoal de Nível Superior” (CAPES) [Finance Code 001] and “Conselho Nacional de Desenvolvimento Científico e Tecnológico” (CNPq) [project numbers 315092/2020-3 and 141111/2020-8].
Declaration of Competing Interest
The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.
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