Abstract:Abstract:One of the concerns for economical production of ethanol from biomass is the large volume and high cost of the cellulolytic enzymes used to convert biomass into fermentable sugars. The presence of acetyl groups in hemicellulose and lignin in plant cell walls reduces accessibility of biomass to the enzymes and makes conversion a slow process. In addition to low enzyme accessibility, a rapid deactivation of cellulases during biomass hydrolysis can be another factor contributing to the low sugar recovery… Show more
“…Some enzyme and substrate pairs are given in Table 7 with the effect of increasing substrate concentration. The agricultural residues (corn stover, Kumar and Wyman (2008) GC-220 Cellulose Increased with increase in conc Kumar and Wyman (2008) Cellulase Avicel Decreased with increase in conc Eckard et al (2013) Cellulases Pretreated forest wood Increased with increase in conc Matsakas et al (2018) Celluclast 1.5 L T. reesei Corn stover and corn fiber Increased with increase in conc Arantes and Saddler (2011) Cellic CTec 2 High CrI cellulose Increased with increase in conc Li et al (2018) corn fiber, rice husk, wheat straw, etc.) needs considerably lower protein loadings to achieve optimum adsorption than the forestry residues (poplar, Douglas fir and lodgepole pine).…”
For the production of biofuel (bioethanol), enzymatic adsorption onto a lignocellulosic biomass surface is a prior condition for the enzymatic hydrolysis process to occur. Lignocellulosic substances are mainly composed of cellulose, hemicellulose and lignin. The polysaccharide matrix (cellulose and hemicellulose) is capable of producing bioethanol. Therefore, lignin is removed or its concentration is reduced from the adsorption substrates by pretreatments. Selected enzymes are used for the production of reducing sugars from cellulosic materials, which in turn are converted to bioethanol. Adsorption of enzymes onto the substrate surface is a complicated process. A large number of research have been performed on the adsorption process, but little has been done to understand the mechanism of adsorption process. This article reviews the mechanisms of adsorption of enzymes onto the biomass surfaces. A conceptual adsorption mechanism is presented which will fill the gaps in literature and help researchers and industry to use adsorption more efficiently. The process of enzymatic adsorption starts with the reciprocal interplay of enzymes and substrates and ends with the establishment of molecular and cellular binding. The kinetics of an enzymatic reaction is almost the same as that of a characteristic chemical catalytic reaction. The influencing factors discussed in detail are: surface characteristics of the participating materials, the environmental factors, such as the associated flow conditions, temperature, concentration, etc. Pretreatment of lignocellulosic materials and optimum range of shear force and temperature for getting better results of adsorption are recommended.
“…Some enzyme and substrate pairs are given in Table 7 with the effect of increasing substrate concentration. The agricultural residues (corn stover, Kumar and Wyman (2008) GC-220 Cellulose Increased with increase in conc Kumar and Wyman (2008) Cellulase Avicel Decreased with increase in conc Eckard et al (2013) Cellulases Pretreated forest wood Increased with increase in conc Matsakas et al (2018) Celluclast 1.5 L T. reesei Corn stover and corn fiber Increased with increase in conc Arantes and Saddler (2011) Cellic CTec 2 High CrI cellulose Increased with increase in conc Li et al (2018) corn fiber, rice husk, wheat straw, etc.) needs considerably lower protein loadings to achieve optimum adsorption than the forestry residues (poplar, Douglas fir and lodgepole pine).…”
For the production of biofuel (bioethanol), enzymatic adsorption onto a lignocellulosic biomass surface is a prior condition for the enzymatic hydrolysis process to occur. Lignocellulosic substances are mainly composed of cellulose, hemicellulose and lignin. The polysaccharide matrix (cellulose and hemicellulose) is capable of producing bioethanol. Therefore, lignin is removed or its concentration is reduced from the adsorption substrates by pretreatments. Selected enzymes are used for the production of reducing sugars from cellulosic materials, which in turn are converted to bioethanol. Adsorption of enzymes onto the substrate surface is a complicated process. A large number of research have been performed on the adsorption process, but little has been done to understand the mechanism of adsorption process. This article reviews the mechanisms of adsorption of enzymes onto the biomass surfaces. A conceptual adsorption mechanism is presented which will fill the gaps in literature and help researchers and industry to use adsorption more efficiently. The process of enzymatic adsorption starts with the reciprocal interplay of enzymes and substrates and ends with the establishment of molecular and cellular binding. The kinetics of an enzymatic reaction is almost the same as that of a characteristic chemical catalytic reaction. The influencing factors discussed in detail are: surface characteristics of the participating materials, the environmental factors, such as the associated flow conditions, temperature, concentration, etc. Pretreatment of lignocellulosic materials and optimum range of shear force and temperature for getting better results of adsorption are recommended.
“…The macromolecular architecture and consequently the accessibility of certain functional groups of insoluble lignin fractions play important roles on the inhibiting effect of lignin. Low molecular weight and hydrophilic/amphipathic fractions of lignin (Leskinen et al 2017) may act in similar fashion as some nonionic surfactants that increase saccharification yields (Eckard et al 2013). Lignin fractions that possess weak interactions with enzymes reduce irreversible binding of enzymes on specific cellulose surfaces.…”
Section: Presence Of Lignin As a Saccharificationenhancing Factormentioning
confidence: 99%
“…Enzymatic saccharification assays should be conducted using "reasonably low" cellulase dosages because excess amount of enzymes can cover lignin and hide detrimental non-productive adsorptive loss of activity (Shen et al 2016). Viable cellulosic bioethanol production likely requires cellulase dosages below 5 FPU/g dry substrate, and it is this range where greatest benefits from process optimization or utilization of lignin blocking additives can be seen (Eckard et al 2013;Leskinen et al 2015b). Better understanding of the interactions that drive enzyme binding to lignin would call for more studies that employ well characterized lignins and pure enzymes with engineered structures that would allow monitoring of binding properties caused by targeted modification of eventually identified binding hotspots.…”
Section: Perspective and Recommendations On Future Directionsmentioning
The main target of a biorefinery pretreatment process is to break down the ligninreinforced plant cell wall structure prior to enzymatic hydrolysis of polysaccharides to fermentable sugars. Various physico-chemical alterations occur in lignin during the biomass pretreatment, but effects of those structural changes on subsequent enzymatic hydrolysis have remained ambiguous. We review the reinforcing and detrimental lignin-enzyme interactions and their underlying mechanisms, and use this structure-function information to assess critical features of current and emerging pretreatment technologies. Our perspective is that truly multidisciplinary research is needed to develop pretreatments that render lignin non-inhibiting to enzymes and with high potential for further valorisation.
“…In addition to lignin disposal in the pulp industry, another major goal in this field is the development of green and efficient methods to transform lignin into fuels and high value-added chemicals [10][11][12]. The polymeric structure of lignin provides an attractive renewable source of aromatic chemicals [13,14]. Catalysis is regarded as a key technology to fulfil the promise of lignin valorization.…”
Lignin and other colored structures need to be bleached after the Kraft process in the pulp industry. Development of environmentally-safe bleaching catalysts or electrocatalysts constitutes an attractive strategy for selective removal of lignin. Seven manganese(III)-complexes with Schiff base ligands 1–7 were synthetized and characterized by different analytical and spectroscopic techniques. The tetragonally elongated octahedral geometry for the manganese coordination sphere and the global µ-aquo dimeric structure were revealed by X-ray diffraction (XRD) studies for 1, Mn2L12(H2O)2(N(CN)2)2 (N(CN)2 = dicyanamide). Complexes 1–4 behave as more efficient peroxidase mimics as compared to 5–7. Electrochemical oxidation of the lignin model veratrylalcohol (VA) to veratrylaldehyde (VAH) is efficiently catalyzed by a type of dimanganese(III) complexes in a chlorine-free medium. The electrocatalytic reaction proceeds through the oxidation of chloride into hypochlorite at alkaline pH along with the formation of hydrogen from water as a subproduct.
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