Simultaneous saccharification and fermentation of cellulose to lactic acid

Recent interest in the industrial manufacture of ethanol and other organic chemicals from biomass has led to the utilization of surplus grain and cane juice as a fermentation feedstock. Since those starting materials are also foods, they are expensive. As an alternative, cellulosic substances-the most abundant renewable resources on earth(1)-have long been considered for conversion to readily utilizable hydrolyzates.(2, 3)For the production of ethanol from cellulose, we have proposed the simultaneous saccharification and fermentation (SSF) process.(4) In SSF, enzymatic cellulose hydrolysis and glucose fermentation to ethanol by yeast proceed simultaneously within one vessel. The process advantages-reduced reactor volume and faster saccharification rates-have been confirmed by many researchers.(5-8) During SSF, the faster saccharification rates result because the glucose product is immediately removed, considerably diminishing its inhibitory effect on the cellulase system.(9)To effectively apply the SSF method to produce substances fermented from glucose, several conditions should be satisfied. One is coincident enzymatic hydrolysis and fermentation conditions, such as pH and temperature. The other is that cellulase inhibition by the final product is less than that by glucose and/or cellobiose. One of us has reported that acetic acid, citric acid, itaconic acid, alpha-ketoglutaric acid, lactic acid, and succinic acid scarcely inhibit cellulase.(10) This suggests that if the microorganisms which produce these organic acids were compatible with cellulase reaction conditions, the organic acids could be produced efficiently from cellulosic substrates by SSF.In this article, the successful application of SSF to lactic acid production from cellulose is reported. Though there have been several reports of direct cellulose conversion to organic acids by anaerobes such as Clostridium, only trace amounts of lactic acid were detected in the fermentation medium among the low-molecular-weight fatty acid components.(11-13) Lactic acid is one of the most important organic acids and has a wide range of food-related and industrial applications.     

Augmentation of the biodisposition of simple sugars from sorghum biomass mediated with biotechnologic processes

The results of the enzymatic hydrolysis of pectin, hemicellulose and cellulose in the biomass of sweet sorghum (Sorghum vulgare var. saccharatum, L.) are reported. Some commercial enzymatic preparations were used: Maxazym CL 2000 (with prevailing cellulase activity), Rapidase C 80 (with prevailing pectinase activity) Rohament PC (mainly with pectinase and cellulase activities) and Rohament O (mainly with pectinase and hemicellulase activities). The treatment with Rohament PC, Rohament O and Rapidase C 80 gives an increase of the glucose content higher than the effect induced by Maxazym CL 2000. On the other hand, the cellulase and pectinase combined treatment (Maxazym CL 2000 + Rapidase C 80 or Maxazym CL 2000 + Rohament O) shows a good synergistic effect in the degradation of the plant cell wall cellulosic material.     

Features of promising technologies for pretreatment of lignocellulosic biomass

Cellulosic plant material represents an as-of-yet untapped source of fermentable sugars for significant industrial use. Many physio-chemical structural and compositional factors hinder the enzymatic digestibility of cellulose present in lignocellulosic biomass. The goal of any pretreatment technology is to alter or remove structural and compositional impediments to hydrolysis in order to improve the rate of enzyme hydrolysis and increase yields of fermentable sugars from cellulose or hemicellulose. These methods cause physical and/or chemical changes in the plant biomass in order to achieve this result. Experimental investigation of physical changes and chemical reactions that occur during pretreatment is required for the development of effective and mechanistic models that can be used for the rational design of pretreatment processes. Furthermore, pretreatment processing conditions must be tailored to the specific chemical and structural composition of the various, and variable, sources of lignocellulosic biomass. This paper reviews process parameters and their fundamental modes of action for promising pretreatment methods.     

Detrimental effect of cellulose oxidation on cellulose hydrolysis by cellulase

To effectively convert complex and recalcitrant biomass carbohydrates to simple platform sugars useful for fuel and chemicals production, mechanical or chemical pre-treatments are often required to make the carbohydrates more accessible for enzymatic hydrolysis. Due to their harsh conditions, some pre-treatments might negatively affect enzymatic hydrolysis because of events such as cellulose oxidation. To study how oxidative modification may impact cellulose's reactivity toward hydrolysis by cellulases, we prepared three cellulose substrates by cupric ion and hypochlorite oxidations, and subjected the derived celluloses to hydrolysis by various cellobiohydrolases from glycoside hydrolase families 6 and 7, and one cellulolytic Hypocrea jecorina extracellular enzyme mixture. We observed a profound decrease of enzymatic hydrolysis on the oxidized celluloses. The effect was attributed to the interference, from oxidized functional groups in cellulose, on its binding/activation in the active pocket/tunnel of cellobiohydrolases. Potential implication of the observed effect from cellulose oxidation on pre-treatment optimization and cellulase improvement was discussed.     

Quantification of morphochemical changes during in situ enzymatic hydrolysis of individual biomass particles based on autofluorescence imaging

Enzymatic hydrolysis of biomass is an established method for producing biofuels. Lignocellulosic biomass such as corn stover is very inhomogeneous material with big variation on conversion rates between individual particles therefore leading to variable recalcitrance results. In this study, we used noninvasive optical microscopy techniques, such as two-photon microscopy and fluorescence lifetime imaging microscopy, to visualize and analyze morphological and chemical changes of individual corn stover particles pretreated with sulfuric acid during hydrolysis. Morphochemical changes were interpreted based on the fluorescence properties of isolated building blocks of plant cell wall, such as cellulose, hemicellulose, and lignin. Enzymatic hydrolysis resulted in particle size reduction, side wall collapse, decrease of second harmonic signal from cellulose, redshifting of autofluorescence emission, and lifetime decrease attributed to the relative increase of lignin. Based on these observations, tracking compositional change after hydrolysis of individual particles was accomplished. The methodologies developed offer a paradigm for imaging and analyzing enzymatic hydrolysis in vitro and in situ, which could be used for screening enzymes cocktails targeting specific recalcitrant structures or investigating locally enzyme anti-inhibitory agents.     

Kinetics of the enzymatic hydrolysis of cellulose: 2. A mathematical model for the process in a plug-flow column reactor

The kinetics of enzymatic cellulose hydrolysis in a plug-flow column reactor catalysed by cellulases [see 1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] from Trichoderma longibrachiatum adsorbed on cellulose surface have been studied. The maximum substrate conversion achieved was 90–94%. The possibility of enzyme recovery for a reactor of this type is discussed. A mathematical model for enzymatic cellulose hydrolysis in a plug-flow column reactor has been developed. The model allows for the component composition of the cellulase complex, adsorption of cellulases on the substrate surface, inhibition by reaction products, changes in cellulose reactivity and the inactivation of enzymes in the course of hydrolysis. The model affords a reliable prediction of the kinetics of d-glucose and cellobiose formation from cellulose in a column reactor as well as the degree of substrate conversion and reactor productivity with various amounts of adsorbed enzymes and at various flow rates.     

Comparative Histochemical Analysis of Cell Wall Polysaccharides by Enzymatic and Chemical Extractions of Two Fruits

A protocol for extracting polysaccharides from cell walls has been modified and used to analyze histochemically two fruits with opposite characteristics. Grapes are nonclimacteric fruits and are harvested at full maturity. In contrast, kiwi fruits are climacteric and are harvested and consumed before they are physiologically mature. The two fruits were analyzed histochemically using two protocols. One method is defined as chemical, and is based on subsequential extractions of pectins by chemical agents. The other is defined as enzymatic because it removes pectins using pectinase followed by hot ammonium oxalate. In both protocols, two types of hemicellulosic polymers are removed by 1 M and 4 M/KOH leaving a cellulosic residue on the slide. Both protocols remove the same amount of pectins, thus confirming their precision. The sum of hemicellulose and the cellulosic insoluble residue are equivalent using the two methods, but the relative amounts of the cellulose and hemicellulosic polymers were dependent upon the method of extraction. When the enzyme was used to extract the pectins, there was less cellulose and more hemicellulose. The removal of polysaccharides by ammonium oxalate and by guanidinethio-cyanate in the enzymatic and the chemical protocols, respectively, yielded approximately the same amount of removed material.

Similar results were obtained from both fruits. Grape, being softer than kiwi fruit, was relatively richer in pectic substances and less rich in hemicellulose and cellulose polymers. No difference in cell wall material could be ascribed to the different ripening habits.     

Comparative Histochemical Analysis of Cell Wall Polysaccharides by Enzymatic and Chemical Extractions of Two Fruits

A protocol for extracting polysaccharides from cell walls has been modified and used to analyze histochemically two fruits with opposite characteristics. Grapes are nonclimacteric fruits and are harvested at full maturity. In contrast, kiwi fruits are climacteric and are harvested and consumed before they are physiologically mature. The two fruits were analyzed histochemically using two protocols. One method is defined as chemical, and is based on subsequential extractions of pectins by chemical agents. The other is defined as enzymatic because it removes pectins using pectinase followed by hot ammonium oxalate. In both protocols, two types of hemicellulosic polymers are removed by 1 M and 4 M/KOH leaving a cellulosic residue on the slide. Both protocols remove the same amount of pectins, thus confirming their precision. The sum of hemicellulose and the cellulosic insoluble residue are equivalent using the two methods, but the relative amounts of the cellulose and hemicellulosic polymers were dependent upon the method of extraction. When the enzyme was used to extract the pectins, there was less cellulose and more hemicellulose. The removal of polysaccharides by ammonium oxalate and by guanidinethio-cyanate in the enzymatic and the chemical protocols, respectively, yielded approximately the same amount of removed material.

Similar results were obtained from both fruits. Grape, being softer than kiwi fruit, was relatively richer in pectic substances and less rich in hemicellulose and cellulose polymers. No difference in cell wall material could be ascribed to the different ripening habits.     

Changes in the enzymatic hydrolysis rate of Avicel cellulose with conversion

The slow down in enzymatic hydrolysis of cellulose with conversion has often been attributed to declining reactivity of the substrate as the more easily reacted material is thought to be consumed preferentially. To better understand the cause of this phenomenon, the enzymatic reaction of the nearly pure cellulose in Avicel was interrupted over the course of nearly complete hydrolysis. Then, the solids were treated with proteinase to degrade the cellulase enzymes remaining on the solid surface, followed by proteinase inhibitors to inactive the proteinase and successive washing with water, 1.0 M NaCl solution, and water. Next, fresh cellulase and buffer were added to the solids to restart hydrolysis. The rate of cellulose hydrolysis, expressed as a percent of substrate remaining at that time, was approximately constant over a wide range of conversions for restart experiments but declined continually with conversion for uninterrupted hydrolysis. Furthermore, the cellulose hydrolysis rate per adsorbed enzyme was approximately constant for the restart procedure but declined with conversion when enzymes were left to react. Thus, the drop off in reaction rate for uninterrupted cellulose digestion by enzymes could not be attributed to changes in substrate reactivity, suggesting that other effects such as enzymes getting "stuck" or otherwise slowing down may be responsible.     

Improved accessibility and reactivity of dissolving pulp for the viscose process: pretreatment with monocomponent endoglucanase

A high accessibility is an essential prerequisite for a homogeneous substitution of cellulose material. In this study, chemical and enzymatic pretreatments to increase the accessibility of cellulose materials have been investigated. Dissolving pulp has been treated with a monocomponent endoglucanase. Fock's method, a microscale process similar to the viscose process, showed an increase in cellulose yield. Simultaneously, the viscosity decreased. To clarify whether the increase in reactivity was due solely to the decrease in the degree of polymerization, the dissolving pulp was also subjected to acid hydrolysis. At a given viscosity level, the enzymatic pretreated pulp had a higher reactivity than the pulp subjected to acid hydrolysis. To achieve 100% reactivity, according to Fock, the acid-treated pulp showed a lower molecular weight compared to the enzymatic-treated pulp. A monocomponent endoglucanase can thus be used to increase the reactivity and accessibility of dissolving pulp in the viscose process.     

Kinetic studies of enzymatic hydrolysis of insoluble cellulose: analysis of the initial rates

A study was conducted on the kinetics of enzymatic hydrolysis of pure insoluble cellulose using unpurified culture filtrate Trichoderma reesei, with the emphasis on the initial reaction period. The initial hydrolysis rate and extent of enzyme (soluble protein)adsorption, either apparent or initial, were evaluated under various experimental conditions. It has been found that the various mass-transfer steps do not control the overall hydrolysis rate and that the hydrolysis rate is mainly controlled by the surface reaction step promoted by the adsorbed enzyme. It has also been found that the initial hydrolysis rate strongly depends on the initial extent of soluble protein adsorption and the effectiveness of the adsorbed soluble protein to promote the hydrolysis. The initial extent of soluble protein adsorption, in turn, is related to the initial cellulose concentration, enzyme concentration, and specific surface area of cellulose, whereas the effectiveness of the initially adsorbed soluble protein to promote the derived to interrelate these parameters without resorting to the Michaelis-Menten kinetics. The present result appear to imply that the role of enzyme-substrate complex formation should not be ignored in deriving a mechanistic kinetic model for enzymatic hydrolysis of cellulose.     

Restriction of the enzymatic hydrolysis of steam-pretreated spruce by lignin and hemicellulose

The presence of lignin is known to reduce the efficiency of the enzymatic hydrolysis of lignocellulosic raw materials. On the other hand, solubilization of hemicellulose, especially of xylan, is known to enhance the hydrolysis of cellulose. The enzymatic hydrolysis of spruce, recognized among the most challenging lignocellulosic substrates, was studied by commercial and purified enzymes from Trichoderma reesei. Previously, the enzymatic hydrolysis of steam pretreated spruce has been studied mainly by using commercial enzymes and no efforts have been taken to clarify the bottlenecks by using purified enzyme components.Steam-pretreated spruce was hydrolyzed with a mixture of Celluclast and Novozym 188 to obtain a hydrolysis residue, expectedly containing the most resistant components. The pretreated raw material and the hydrolysis residue were analyzed for the enrichment of structural bottlenecks during the hydrolysis. Lignin was removed from these two materials with chlorite delignification method in order to eliminate the limitations caused by lignin. Avicel was used for comparison as a known model substrate. Mixtures of purified enzymes were used to investigate the hydrolysis of the individual carbohydrates: cellulose, glucomannan and xylan in the substrates. The results reveal that factors limiting the hydrolysis are mainly due to the lignin, and to a minor extent by the lack of accessory enzymes. Removal of lignin doubled the hydrolysis degree of the raw material and the residue, and reached close to 100% of the theoretical within 2 days. The presence of xylan seems to limit the hydrolysability, especially of the delignified substrates. The hydrolysis results also revealed significant hemicellulose impurities in the commonly used cellulose model substrate, making it questionable to use Avicel as a model cellulose substrate for hydrolysis experiments.     

Role of supramolecular cellulose structures in enzymatic hydrolysis of plant cell walls

The study of biomass deconstruction by enzymatic hydrolysis has hitherto not focussed on the importance of supramolecular structures of cellulose. In lignocellulose fibres, regions with a different organisation of the microfibrils are present. These regions are called dislocations or slip planes and they are known to be more susceptible to various forms of degradation such as acid hydrolysis. Traditionally the cellulose within these regions has been assumed to be amorphous, but in this study it is shown by use of polarized light microscopy that dislocations are birefringent. This indicates that they have a crystalline organisation. Dislocations may be entry points for endoglucanases. Using a fluorescent labelled endoglucanase combined with confocal fluorescence microscopy, it is shown that the enzyme selectively binds to dislocations during the initial phase of the hydrolysis. Using a commercial cellulase mixture on hydrothermally treated wheat straw, it was found that the fibres were cut into segments corresponding to the sections between the dislocations initially present, as has previously been observed for acid hydrolysis of softwood pulps. The results indicate that dislocations are important during the initial part of enzymatic hydrolysis of cellulose. The implications of this phenomenon have not yet been recognized or explored within cellulosic biofuels.     

植物纤维的水解与SSF过程的数学模型

采用一种植物纤维木糖渣为原料,对纤维素酶水解及同时糖化和发酵（SSF）过程进行了研究,研究结果表明,在纤维素含量为42g.L^-1,纤维素酶的加入量为280FPIU.L^-1,乳酸菌用量为0．5g.L^-1时,乳酸对纤维素的转化率可达80％,并从反应机理及动力学角度出发,建立了纤维素酸水解与SSF过程的数学模型。     

High‐level hemicellulosic arabinose predominately affects lignocellulose crystallinity for genetically enhancing both plant lodging resistance and biomass enzymatic digestibility in rice mutants

Rice is a major food crop with enormous biomass residue for biofuels. As plant cell wall recalcitrance basically decides a costly biomass process, genetic modification of plant cell walls has been regarded as a promising solution. However, due to structural complexity and functional diversity of plant cell walls, it becomes essential to identify the key factors of cell wall modifications that could not much alter plant growth, but cause an enhancement in biomass enzymatic digestibility. To address this issue, we performed systems biology analyses of a total of 36 distinct cell wall mutants of rice. As a result, cellulose crystallinity (CrI) was examined to be the key factor that negatively determines either the biomass enzymatic saccharification upon various chemical pretreatments or the plant lodging resistance, an integrated agronomic trait in plant growth and grain production. Notably, hemicellulosic arabinose (Ara) was detected to be the major factor that negatively affects cellulose CrI probably through its interlinking with β‐1,4‐glucans. In addition, lignin and G monomer also exhibited the positive impact on biomass digestion and lodging resistance. Further characterization of two elite mutants, Osfc17 and Osfc30, showing normal plant growth and high biomass enzymatic digestion in situ and in vitro, revealed the multiple GH9B candidate genes for reducing cellulose CrI and XAT genes for increasing hemicellulosic Ara level. Hence, the results have suggested the potential cell wall modifications for enhancing both biomass enzymatic digestibility and plant lodging resistance by synchronically overexpressing GH9B and XAT genes in rice.     

Adsorption of cellulase on cellulose: Effect of physicochemical properties of cellulose on adsorption and rate of hydrolysis

In the cellulase-cellulose reaction system, the adsorption of cellulase on the solid cellulose substrate was found to be one of the important parameters that govern the enzymatic hydrolysis rate of cellulose. The adsorption of cellulase usually parallels the rate of hydrolysis of cellulose. The affinity for cellulase varies depending on the structural properties of cellulose. Adsorption parameters such as the half-saturation constant, the maximum adsorption constant, and the distribution coefficient for both the cellulase and cellulsoe have been experimentally determined for several substrates. These adsorption parameters vary with the source of cellulose and the pretreatment methods and are correlated with the crystallinity and the specific surface area of cellulose substrates. The changing pattern of adsorption profile of cellulase during the hydrolysis reaction has also been elucidated. For practical utilization of cellulosic materials, the cellulose structural properties and their effects on cellulase adsorption, and the rate of hydrolysis must be taken into consideration.     

Structural properties of cellulose and cellulase reaction mechanism

The effects of structural properties and their changes during cellulose hydrolysis on the enzymatic hydrolysis rate have been studied from the reaction mechanism point of view. Important findings are the following: (1) The crystallinity index (CrI) of partially crystalline cellulose increases as the hydrolysis reaction proceeds, and a significant slowing down of the reaction rate during the enzymatic hydrolysis is, in large part, attributable to this structural change of cellulose substrate. (2) The crystallinity of completely disordered cellulose, like phosphoric-acid-treated cellulose, does not change significantly, and a relatively high hydrolysis rate is maintained during hydrolysis. (3) The specific surface area (SSA) of partially crystalline cellulose decreases significantly during enzymatic hydrolysis while the change in SSA of regenerated cellulose is found to be negligible. (4) The value of degree of polymerization (DP) of highly ordered crystalline cellulose remains practically constant whereas the change in DP of disordered regenerated cellulose is found to be very significant. (5) Combination of these structural effects as well as cellulase adsorption, product inhibition, and cellulase deactivation all have important influence on the rate of cellulase reaction during cellulose hydrolysis. More experimental evidence for a two-phase model, which is based on degradation of cellulose by simultaneous actions of cellulase complex on the crystalline and amorphous phases, has been obtained. Based on experimental results from this study and other results accumulated, the mode of cellulase action and a possible reaction mechanism are proposed.     

Optimization of enzyme complexes for lignocellulose hydrolysis

The ability of a commercial Trichoderma reesei cellulase preparation (Celluclast 1.5L), to hydrolyze the cellulose and xylan components of pretreated corn stover (PCS) was significantly improved by supplementation with three types of crude commercial enzyme preparations nominally enriched in xylanase, pectinase, and beta-glucosidase activity. Although the well-documented relief of product inhibition by beta-glucosidase contributed to the observed improvement in cellulase performance, significant benefits could also be attributed to enzymes components that hydrolyze non-cellulosic polysaccharides. It is suggested that so-called "accessory" enzymes such as xylanase and pectinase stimulate cellulose hydrolysis by removing non-cellulosic polysaccharides that coat cellulose fibers. A high-throughput microassay, in combination with response surface methodology, enabled production of an optimally supplemented enzyme mixture. This mixture allowed for a approximately twofold reduction in the total protein required to reach glucan to glucose and xylan to xylose hydrolysis targets (99% and 88% conversion, respectively), thereby validating this approach towards enzyme improvement and process cost reduction for lignocellulose hydrolysis.     

The cellulolytic system of the termite gut

The demand for the usage of natural renewable polymeric material is increasing in order to satisfy the future needs for energy and chemical precursors. Important steps in the hydrolysis of polymeric material and bioconversion can be performed by microorganisms. Over about 150 million years, termites have optimized their intestinal polysaccharide-degrading symbiosis. In the ecosystem of the “termite gut,” polysaccharides are degraded from lignocellulose, such as cellulose and hemicelluloses, in 1 day, while lignin is only weakly attacked. The understanding of the principles of cellulose degradation in this natural polymer-degrading ecosystem could be helpful for the improvement of the biotechnological hydrolysis and conversion of cellulose, e.g., in the case of biogas production from natural renewable plant material in biogas plants. This review focuses on the present knowledge of the cellulose degradation in the termite gut.